Teale ae Heer aaee 1s alecta bugle dtl HARLIUY SSSR SSS iH Sf 264 — CORNELL UNIVERSITY. M4 (2. 2 1908 THE Roswell P. Flower Library THE GIFT OF ROSWELL P. FLOWER FOR THE USE OF , THE N. Y. STATE VETERINARY COLLE L 18907 ag % re RIBRAR' ‘ornell Universit Cornell University The original of this book is in the Cornell University Library. There are no known copyright restrictions in the United States on the use of the text. http://www. archive.org/details/cu31924001175326 ‘VI ‘SHIVY ‘INTTION ALYLG VMOT ‘ONIaTINgG AUTVG PRINCIPLES AND PRACTICE OF BUTTER-MAKING A TREATISE ON THE CHEMICAL AND PHYSICAL PROPERTIES OF MILK AND ITS COMPONENTS THE HANDLING OF MILK AND CREAM, AND THE MANUFACTURE OF BUTTER THEREFROM BY G. L. McKAY, Professor of Dairying in the Iowa State College, Ames, Ia. AND C. LARSEN, MLS.A. Professor of Dairy Husbandry, So. Dak. State College, Brookings, S D.; formerly Associate Professor, Lowa State College, Ames, Ia. SECOND EDITION, REVISED AND ENLARGED. FIRST THOUSAND NEW YORK JOHN WILEY & SONS Lonpon: CHAPMAN & HALL, Lrwirep 1908. ae Ns ) er 4 Copydaht, 1906, 1908, BY G. L. McKAY anv C. LARSEN The Scientific Press Robert Bewmnwnd and Company New York PREFACE TO SECOND EDITION. THE science of dairying is constantly broadening. The methods and art of manufacturing the best quality of butter have gradually changed in conformity to the scientific princi- ples involved, ard no manufacture of butter should now be undertaken until a careful study has been made of the prin- ciples governing the best methods of manufacture. The authors admit that, in our present state of knowledge and experimental progress, it is in some instances difficult to distinguish well established facts from those not universally confirmed; hence it has been the object of the writers to give only information supported by the preponderance of experi- mental evidence. The first edition of this book has been, in a manner, well received, indicating the work has met with general approval. The second edition has been carefully revised, and two chapters, one on ‘‘Creamery Refrigeration” and one on ‘‘Hconomic Oper- ation of Creameries” have been added to mect an indicated demand, and the authors hope that this will justify the use of the book in our dairy schools, and also as a general reference book for those engaged in dairy pursuits. The authors believe that the subject of dairying should no longer be treated as a whole, and for this reason such subjects as Testing Milk and its Products, Dairy Bacteriology, Cheese- making, and Technology of Milk and its Products, have not been treated comprehensively in this work. In connection with the practical phase of butter-making the writers have iii iv PREFACE, endeavored to give such scientific information related to it as may be of interest and value. The scientific knowledge has been acquired from time to time through work done by various investigators at the different Experiment Stations. To all of these men who have searched for and discovered facts bearing upon dairying the authors wish to express their thanks and acknowledgment. It may be added that the statistics and tables given in this work have been quoted from noted, reliable authorities, as indicated. The authors are also indebted to the following parties for the use of electrotypes: Mower-Harwood Co., and Cherry Bros., Cedar Rapids, Ia.; Creamery Package Co., Waterloo Cream Separator Co., and Iowa Separator Co., Waterloo, Ia.; Vermont Farm Machine Co., Bellows Falls, Vt.; Jensen Mfg. Co., Topeka, Kans.; Ox Fiber Brush Co., Davis Cream Sep- arator Co., Borden & Selleck Co., and De Laval Separator Co., Chicago, Ill; Wagner Glass Works, and J. H. Monrad, New York, N. Y.; Burrell & Co., Little Falls, N. Y.; Empire Cream Separator Co., Bloomfield. N. J.; Dairy Queen Mfg. Co., Flora, Ind.; Dairy Record, St. Paul, Minn., and W. D. Hoard, Fort Atkinson, Wis. G. L. McKay. C. Larsen. CONTENTS. CHAPTER I. PAGE COMPOSITION OF MILK. ..4c0d00 2c ie be des hn wa ecae os ere a dane ba nine ee 1 1 ye fir ition Ole Milke sain ofblancntede Wado aSeeta dace eh ans See 1 2, -Composition-of Milky a ig dee noting Pay dees sauces Sead wiidoaee 2 3. Variation of Total Solids, «.. .-. o0%%daseees ore aciesce eevee aueas 3 he NAR oe a ae oad fos aa eee Li Ba Sie sya ey es dhsee ence taeda hobea tate fad 4 Be Maier MAIS, 2.25qs .danhie 3 setae Geis oe SA Oe a ee Ay et Eesha ae dl 5 6, Properties Of Mati... iat anc cane ony ad Se Ree wR ee acne ee 7 %. Glycerides:of Hat .: scociseseces seed eve tense ao eed ea te haw ews 8 8. Theories in Regard to Films Enveloping Fat-globules.......... 9 9° \ClASs@S: OF RatS 22 cds cd nea cik es akeeaie Ree MOR ARUN Dd ee ee eae 10 Ay Nolatiles joc. ipod heat iee Le tas oe eee aay Ae ee Ce 11 BON onsvolalesc ise vektqusais eo see ee aela de ilt ee ane sak gala tis 12 10. Composition of Butter-fat. 0... eke cence eee eee 13 Wikio (GASES oe ese a etoeel ohare OH a aah bd mee AE! ace ada eds Myuehel alannes area 15 12 MIbUMENs f.2..c404 p dack wad nad os amrieremtadad win te tee Hawn 4k 16 TS sSugarxd dee awe bee aaenade ce des onus sepia tara en Bie ess 16 Vay ASH gc icsank cdties Be cue PANE BAERS HOOT RTS Mts Hee ee eT Sas 18 15, Gases or Taints of Milk. 10.0.0... 2.0 ccc eee cre eee renee 18 16) Coloring Matters: «4. ic< ca eae 4 ae sais eae ad snk s ae eines oe 20 17. Other Constituents of Milk... .. 0... ee eee cece ee eee eens 20 CHAPTER II. Milk SECRETION? jas askiss saa ts daly ae tes os eRe othe Bae eG ies Say ee sl 22 1. Mammary Gland as a Secretory Organ .........eccc eee e eee 22 2. Internal Structure of Cow’s Udder. .......... eee e ee eee eens 22 3. Theories of Milk Secretion. . 2.0.00... cece ccc cee eee tenes 25 4, Conditions Affecting Secretion of Milk................ ee 28 5. External Appearance of Udder..........eseee eee eeeeeneeeee 29 Ge Mile fOVer cs, ance edie cna ahaa adce a sehalels longer davenansiarea aerate Siew oraeed 30 CONTENTS. CHAPTER III. Opacity Of Milkics scccsansts cw cit aeiw ene da nan eee esi ee eS . Chemical Reaction: of Malley. cccciv a eiags ese eleg we nee ay aie es . Specifie Gravity of Milky .ccanss sus nev ed va vies ase ce eae gees Natural Separation of Milk and Cream... .............00000- Acdhesiotr Of MTU sy igs asada se eos mud nop sale bot dab dna pled na hulu Viv tain ade L. Viscosity Of Milk, 4a ctemesdteresowceh ete nd eet eeeee coe eens L. Specihe: Pleat; of Male ices ghia ws tea rea Sede eaten 2% . Effect of High Heat on Properties of Milk... ................ . Destroys nearly all Germs... 2.6... eee cee eee eee . Diminishes Viscosity or Body... ........ 2.0.0 e eee eee Drivessoff GaseSic.c.camie sca te waa vs wate ee eet eee. ,. Imparts a-Cooked Taste... vcs sc vap aes ga Pu Sea arilge aeiees . Precipitates Albuminoid and Ash Contents......... .. . Destroys Properties of Enzymes. ... ......... 0.0 ee eee Divides the Fat-globules. ........... 0.00: cece eee ee eee . Caramelizes the Sugar... 0... 0... cece eee eee eee » General Remarks. «ga: oc x ape lstedten s siena aay o wholes ohana m SOMNANMRWNeR HOOP DoOWS CHAPTER IV. FERMENTS- ON MAGK) 0 ccucnkas cacaa cid adea dened da cum Sewwaltudede her WD ORTUGT ONS, 2 asd vas eles cas silane ry at R Ged als where oy ded Bins mpetslocencteats duis ital ac 2. Size-and Slrape of Bactetiass »2s.5s56deu5s eee sap ceawete yee. 3. Favorable Conditions for Bacterial Growth..............20005 Be. DeMperatine sca we eaaasn tind argu cane dein yieas Bg NTI Stal Bates te ted tm watches ap ay econis eA bates aresathg cae Larlereualte sees! eae . Number of Bacteria in Milk. 10... ck ccc cece eevee rene . Sources of Bacteria in Milk. 2... ccc cece cence WN me CHAPTER V. ANBNORMAG: MGR: 2ccc-ast oae.24 4 Gee d4 eS aueus tnd dade eae beeewten 1. (Colostrum lil tsuniieaainte pent eens s Ged maya swat eee hess De alta MAM s. ss coushansts an atane terials a Wie low aod aces eae eg es aidan ioe Narees 3: Bloody ot Red Milk. .xisc: cece rs aa sie cesta ead eb aia a nmels Be Blue: Mil Kasia so sae eee ed Bale eg lies et had ee Riles nie rade ab we Sky CONTENTS. . Milk from Cows which have been in Milk a Long Period... .... . Milk fron Spayed ‘Cows... 05. .eseeseisvev neu Oareraesteebes i GDODNAN e4 aay + oO a] = ian . Milk: front Bick: Cows ie ss .dscecu's eH aoa e Oe ae ak en SOs CHAPTER VI. VARIATION Of Far in MUIPK..,. ¢¢c4¢csec¥ es ee be eet oo ges oe as Rie ees SOnMANOaAhWNH me Individuality: OF COWS. 5c ais gursunt aed deh d Lda Reeth eee Slee aay 5 BREE. OF COWS: So actanw on Rat EAR eA ROE eka eae Time between Milkings. ..........0. 00.00 cee eee eee eee _ Manner of Milling 'ss gos exiexee eaietsesed ghana xed See oe lees ) Millimesnisehinedis ans cacave senses bee ahs ef apiac dak peneaen dae , Hore Milk and After Milk. .cc: acieaascngme dene ach awe ee eeen Mee: Of COW: c.2%.a yaa the gele Wee eo Bea RHEE Hage es . dactation: Peétiod..s5 dueeekte been gcd eo bee kes cles 4 Saree Sete HOO) Of COWS) 2:05 aulnancate.s oe uitsc ding uaa ne@lees Senury gual week . Environmental Conditions. ...... 0.0... 2c ieee ee ee eee ee CHAPTER VII. RECEIVING, SAMPLING, AND GRADING MILK AND CREAM............. 1. Receiving and Grading of Milk and Cream................... A B C. D E ANION hwh Detection of Abnormal Milk Through the Senses. ....... Use ior Acid RGStS: hve waiisienn ty sing sthyiees Min ee deh ap idlg ances Use of Fermentation Tests. .....0..0..000 0000 cence eee a. Gerber and Wisconsin Curd Tests. .............. Grading Milk by Heating. ................0.0...0000. Use of Babcock Test and Lactometer.............0.0. . Necessity of Good Milky sacs cege ee cee ca gereyancarmesesenees SamplingiOf Mile, a sesacit aa iene ta cuattcae nica Sa Ses Das ». PaMphnis-tubeyg. «russes alee sous sd esle adleneteadle mene oo . Sampling Churned. Milky: cv aecas en sei edeaworewesacese eds Brozen. Milly ve 6 ve ss gees eee wera cawtyseeave aes ube ees tee . Sour and Coagulated Milk. 2... c5.c04 ssce: se we teawec es we one Apportioning Skimmed Milk... 2.0... oe eee eee eee CHAPTER VIII. CoMPpoSITE SAMPLES. ..........- Sciseissgssiiboud: a 4 ula Geena dena asayivend aoe wnbael Dib lnah oe Te DefnitiOns oa 9.c-0G davon cdae hehe wiadies cadens need eee thane 4 99 99 vill CONTENTS. PAGE 3. Kind of Preservatives to Add. 2.2... 0... cc cece eee eee eee 99 4, Arrangement of Composite Samples... ............ 00000 e eee 102 5. Care of Composite Samples. ... 0.0.0... eee eee eee 102 6. Asieragé Samples. caro. duet avmee ed mas becedcen Ce smaee¥a wiegcd se 104 7. Composite Sampling without the Use of Preservatives......... 104 CHAPTER IX, CREAMBERY ‘CALCULATIONS vv go tals ioe add ade sh gO guard gan Mela oe des pe GO 105 1. Finding Average Percentage of Fat... 2.0.0... 00. cece eee eee 105 2. Caleulation, OF OVerrii p..2 psc scone Gag hacen Sa ero S EAA 107 A, Thoroughness of Skimming... ............0000 00 eee ee 108 B. Completeness of Churning. ........-.....-..000 0-0 108 C. General Losses in Creameries. ........... 00000000020 ee 108 D. Composition of Butter Manufactured. ................. 108 8. Calculation of Churn-yield. .......... 0.0.0.0 cee cece eee eee eee 109 4. Calculation, Of Dividends: ncou4aeawa eee bad Qe namede aa Rea w eee 109 5. Cream-raising Coefficient... . 0.2.00... 000. eee eee 113 G, ‘Statement! toPatrons, . g%2. ys: sya rina ea eR ean Gea pee es wR 113 7. Paying for Fat in Cream as Compared with Paving for Fat in Milk 116 8. Degree of Justice in Paying Cream Patrons More per Pound of Hat than the: Mik Batronsy, ...s.. 2 ceed b wun pee nee eoe le aS wee 117 CHAPTER NX, Heatina MitK PREVIOUS TO SKIMMING... 0.0.0.0. ccc ee eee ee eens 118 1. Reasons for H@Sting: con ces sc ies nosey weduyue ees awntianaaves 118 2. Advantages of Warming Milk to High Heat Previous to Skim- MINGS &, \iicietpraas Seameed wee se pegs Gere ye kako RR me 119 By LLOW PLCAUCC Sy eevee asal vera des Hie ueaenciaeateoden, deaths ese a. kites eaatals 121 CHAPTER XI. SEPARATION ‘OF CREA 9 sce gins $44 ae eg eed v4 BREE BETS Ra ee a ads 123 1. Grayitye Greaininigy yok we esd 4 peace eee od ah vs dea ane a 123 A. Shallow-pan System, 2.000.000. 0c cece eee e eee ees 123 B. Deep-setting System. 2.0.0.6... cece eee enna 124 a, Probable Explanation... ............0.00000000- 126 C. Water-dilution Cream (Hydraulic). ...............000. 128 2. Centrifugal Creaming............0. 00000 c cece cece eee eeeeee 129 As Awantagess: © casa stain «Match nis & paltaee nde Owed Se aes 129 B. History of Centrifugal Separators. .......0.....0000005 130 Cl” Modern: Séparators: s.cssan awe coder cs aes end eee toe Sas 132 D. Classification of Separators.............000cc cece ee eee 133 CONTENTS. ix PAGE E, Process of Separation. « « ¢.24 0:44 a ceadevssevesaunees 134 F, Relative Amount and Richness of Milk and Cream QO Paine eee gaan An tadaenn ean nap dese RE 137 a, Regulation of the Cream or Skimmed-milk *crew. 137 b; Rate of Inflow: s24245) on See ersee ce Geeere ytnen 138 Gee SPCC O 3s, Meee Na stig ah nassau ile aod MORE hayerte Migr 138 d@. Temperature: .ci.¢eedenecigsesaperiaaea ads 139 G, Conditions Affecting Efficiency of Separators........... 139 a. Manner of Heating Milk... .......0........... 139 b. Condition of the Milk... ...........00..0 0000000. 141 c. Overfeeding the Separator..................200. 141 Gs SPCC y oie 5 2 sei aipgwcie Ma age Wide +a Bier see 142 e. Steadiness in Running......................00. 143 fF. Thickness of Creams... 2. cages ie eese pee naib ee 144 g: Slushin Bowl... ndsdenteada seals aancanseaancn 144 h, General Remarks. ... .........0 02-0 s cece eeeees 145 CHAPTER NII. Harm SEPARATORS ja. wise cede ew a eeenins eens Mea Reged weed 146 1. Introduction of Farm Separators... 22.2... eee 146 2. Reasons for Introducing Farm Separators..............-06-. 147 3. Objections to Farm Separators. ...... 00.00.2200 2 eee eee 152 4, Thickness: 6f Créamit. ccs sx acc aa vues Geen yes REV SRA NORMS 152 5. Power for Farm Separators... 2.0.0... 0c cece eee 155 6. Care of Cream on the Farm............. 0.00 c cece ees 158 7, Disposition Of Creat, cygeuca.wakewic ane and God alas Ge Gand saa eee 167 A, Shipping Of Cream. vac. ess cease eae canw anced acawe ioe 169 B. Making Butter onthe Farm................0......00, 169 CHAPTER NIII. PUSTEURIZATION: & died acd Sa Rdoder aces bled Rady SR GaSe iG vee RP adi 173 1. Definitions yy pesesoo tose dw dede rer dulce ee Aa Bae 173 2. Methods of Pasteurization, ......... 0.6.00. cee cee ee eee 173 A, Intermittent. vac caa peers seus cay nes BS dese das ees 4 173 Bi - COMPA UOUS: fy i5o ine ais balavers oka Riga ee ans wtarmaerseale Gare aeS 174 3. Selection of Pasteurizers. . 0.2.0... eee eee 175 A. Durabilityvand Capacityis cs conisasen eres nae « 175 B. Economic Efficiency... 0... .. 2. cc cece cee eee eee 175 @., HORI SUPTACE: by a ba een cscs Fe Es 176 b. Degree of Adhesiveness.. 1 ........ 000-0 ee eee 177 c. Thickness of Layer of Condensed Steam.......... 180 d. Difference in Temperature on Each Side of Heat- MNS SUTLACE 2 oes i aims saan 4 dia sbreeee neues aon 181 x CONTENTS. PAGE e. Proper Utilization of Steam Turned into the Pas- OUTIL Da ie-tagng mine ie avai) Boeri tace Seal Seg ahi cae ed 182 C. The Cost of Pasteurization. ........... 0.00.00. e eee eee 183 D. Advancement of Pasteurization. ................2..000. 183 E, Advantages of Pasteurization. .....0......0 0c e eee 1s4 FE. Disadvantages of Pasteurization... ..............-.00. 186 CHAPTER NIV. CREAMARIPENINGscvase 44 in eae oe seeet ge Mebane hada aeebana meee 187 1, WDehniiOniy +s) ue a kayes aide iaw eee mies else a eee tedisige + 1S7 2, Objects: of Cream-ripemime: 2... ;csocwes ered dese useeQiseveniy 187 A. Production of Flavor and Aroma... ................004 187 B. Increases the Churnability of Cream... ..........2-.4.- 191 C. Increases the Keeping Quality of Butter............... 192 3. Ripening Temperature of Cream... ..........6. 0005.00 eee eae 194 4. Amount of Starter to Add to Cream. .. 2.0... eee 196 5. Stirring of Cream during Ripening. ......... go ab Dales uoares 197 Gs Natural: Pupemiige cae sane dopa geaerg oe wie rad ean 4 CaS 198 7 Nata ficial SRA 1A gh cpa 5 Sle a echgs sarah eh gegen 9 stan adadadehh GG bala DRM Se 199 8. Ripening Cream when Churning is Done Every Other Day... .. 201 9. Nisine Of Cr@ai. ig cc de Sah eb gee tok HS Rew GaSe wae ee ew 202 A MOUATINe OR Creams whi ag aks a phage ease eeesnaw ene 203 By Wind of Matkets ccc gases karan de neces gaan soa da na Zee 204 Cs Amount ol Cream): caec genni ea ee area adminis he manliga aeeees 204 D. General Creamery Conditions...............0..022000. 205 10. Examining and Testing Cream for Acidity during Ripening. ... 205 ‘iL’, ANTM S: SESE 1. m ehh nee e te euhieh aaah 5.8 rca tanh NSO Gyectett A gol Wh ake co 206 2k: TAUPE GROIN S! LES ties dpc ne: genase ait tal 6 dear ead g dente a a Had a ie Eg 208 13. Amount of Acid to Develop. ........0..0. 0.000. c eee ce eens 208 tay Chances in Cred... var daver Sones wears were Boe et Gace s 210 wy /PhVSI@al. nord bale eas 228 Hie gu GFE Mos Weed wand gas 210 Bs Biologia: ag Gta isha gives Wiel ae & auton Relea een darkaee 210 Gy (Chemica), cecnaxiian Aeeeiet AG aaa n owen 8 pean eke ¥ pleas 211 CHAPTER NY. STA TRISTE S lan fe lamces wld Sniecd dow nace vodig Goweunn a dane a Big laa eee GNI 4g. ante ies 216 Ls DEANITLOTIR 44-8. alae wad & Ronen ks BAeAe GM edn bad onde as 216 D> FU SUOTY hod oe: woe sue wien ak laa Banh naate ane aR awa Wes teres a 216 8. Classification of Starters... 0.0.0... 0. cece cece eee eeees 216 4. Preparation of Natural Starters........0 00.0... eee e eee ee eee 217 5. Commercial Starters or Pure Cultures... 2.2.0.0... 000.0000 217 6. Preparation of Commercial Starters..............00006 hte DES PF, WH OGULAHTO No tsege ais: Wasa Bite HEA See BN ave corlerre vahlagtednie as Gee Ea ee 220 CONTENTS. xi PAGE 8. Length of Time a Starter Can be Carried............0.00.00 00 222 9: POOPISUAREENS! 22.1. os ade ne aS SORE ERG aS Gwen aera’ 223 10. Under-ripening and Over-ripening of Starters... ........000- 223 11. Amount of Starter to Use... 0... ce cee eee 224 12): Usé- Of Starter Can's.3.4oacaulas Gitelnk Saene thas ea ewlee Bake ne Reta y 225 CHAPTER XVI. CHURNING AND WASHING BUTTER. .......... 0000: cece cece e neces 226 Le Wehinitiony a: 446 ecu deeek eee ed ee eee SOL e es eee Re ke 226) 2, Conditions Affecting the Churnability of Cream. .............. 227 Au TOMMPSPO CUES, 124 oa cance atlas Gubsnann hae dh aubleha Roane eveomss ages 227 B. Richness of Cream... 1.0... 0000.0 c cece eee nee eens 231 C. Amount of Cream in Churn. .......... 00.000 cece eee 233 1D; Degree of Ripeness: wia ce suc. ea ease desde eke os 234 Hy Nature OF AGI at NOM. 325 mas diy-ertdans on tatnns Melee eet 235 F. Size of Fat-globules.. 1.2.02... 0. eee eee cence nee 236 3. Strainine Of Creatives sac waite das Gero s'k/occu dla sere es ata wen eeeas 238 A COLO sc yeh eo eda Rah DR AS Pe LSE aed ae washed kos oan: 238 5. When to Stop the Churning Process. .............00.00.00008 239 6. Churning Mixed, Sweet, and Sour Cream... .......0.2.0...0.. 243 7 Ditneult Churnime:, » 2s. sack wales eee cake ks ed eek ee 6 243 8. Keeping Churn in Sweet Condition. ......................00. 245 9. WWashiner of I whter. 0 Sy ocacte ce tal Sanat ee ancy, BPaligd edie Gud Bk 247 A. Purpose:0f Washingicc ais casi iea cere pO Lea Ranwsneaes 247 B. Temperature of Wash-water.... 0.0.00... 00.0.0. ee eee 247 C. Kind of Wash-water to Use... 0.0.00... 0 00 eee 248 10. Methods of Purifying Wash-water.............0. 0... 000000.. 250 A, PilGRatlOn’ 2) ath eres hg bap iaes ual anos eno uEs Sun GanahAe eee 250 ds. COMTMUOUSS 2.6 +e eiee ey ee RE SRE eae tee meee 253 bs. Lint Srimitt Crit aac. covets wei Re ace eos awe onli ese aloe 254 Bi Pasteurization. 24.24 Abe Sey oo ee dae ee ass Sete ees ces 250 11. Advantages of Purification of Wash-water................00. 255 CHAPTER NVITI. SALTING AND WORKING OF BUTTER.......... 000. c cece e eee eens 256 1. Amount of Salt to Use to Produce Proper Flavor............. 256 2. Effects of Salt upon Keeping Properties... ...............6-. 258 3. Salt Facilitates the Removal of Buttermilk. .................. 259 4, Salt in Relation to Water in Butter... ...............000000- 259 5s Gritty Butter: 3 atite.cawenpon aneards dds cake Sova nod 263 6. Mottled! Butters. caiece an ciainas deg aie RR Anka eee ower ae aed apenas 263 7, MNe-SaltnGs 4 .54cewesaed SSSa iss OE ME er ee de Ee wey as GSede 264 8. Objects of Working Butter... ...... 0... c cece eee eee eee eee 266 CONTENTS CHAPTER XVIIL PACKING AND MARKETING BUTTER .. .ececceuccccvececccecevcercs d- Kind! of Packupe tO: Use: ciacgg anos dase tidy swan eeneieroe 6 Uae 2: UPreparatlonot Lubses vs. sis sages Mawes Seles gaits aes ee eels 2M aQmr Ww Packing of Butter. 0 cose ce tacte edd aeemiede ee ee ee Gee sas . Packing Butter for Exhibition Purposes. ...........00 eee eee . Storing Butter in Creameries... 00.0.0... cece cece ee eee eens . Cost of Producing One Pound of Butter... ..... ccc eee e eee eee CHAPTER NIX, COMPOSITION’ OF: BUTTER) oo cg0 cine dei ses va ug nse we ee WRG sould en nee eo 1, Average: Composition: ii6 ciara cd ea eee sak Galen ae hae oe 2. Effect of Composition of Butter on Quality... .............0-, A; Curd Bnd Sugars i neceooida eas seat pene e anes Goons CHAPTER XX, JUDGING AND GRADING BUTTER. ...... ccc cece cece eee ee eee eeeees 1, Standard. for Judging: oo. ccussue cedae essa sede rece eeneeya 26 Manner of JMG GING) ces esac cuaodsaven bear oeaeaad eee ea aees DAS BOC V itd anes aceite aie acyals aomaenn a hdtiecd bths SAE Me © hleiaCiepulad Be Be HAVOR 208 ode dance bam tabbed aw Someone onwa canada CS COLOR Gare sar occa erat g Shes ern tao wa alle aw RE ote aR nresasiued 9 aati a DD: Ball tint negcateuy ate wie arias naan tee nama om wean ee eee HOw he Wh GS LCs gaa a oe ahs aes cee gle a ad abst aod aedegrdon ub valde wed eect’ 3. ‘Classification Of Butter’ oso o0.5 a6 oeaaeahaed thew 8 mel ad wild ars 4. Grades Of Butters. cic scca au ccs te ee RR away oe gen Yew cudhte Ghats dhe Coouine Faciuitres FoR CREAMERIES..... 1. Cooling Systems......... b Spt: suc aNa aesth a4 2. Natural Ice-system ................... A. IXind of Ice-house........ : B. Size and Shape of Ice-house C. Filling the Ice-house...... D. Source of Ice 3. Usage of Ice in Cooling Cream CHAPTER XNXI. A. Directly. B. Indirectly CONTENTS. Xilk 4. Mechanical Rofrigeration.............00 0000.00 eeeeeee 323 A. Application of, in Creameries..................... 323 B. Chemicals Used for Mechanical Refrigeration. ....... 324 C. Principles of Producing Cold Artificially. ........... 324 a. Compression. b. Condensation. c. Expansion. D. Transferring the Cold. o:3 6 ci deeaveu tev sass oak cana 326 CHAPTER XXII, EXcoNOMIC OPERATION OF CREAMERY...........0 0000 ce cee eveuee 329 1, Hiring: the Boilers :2.s 0 cereus toi e ie cigs mae Seow era ane en 329 2, Burning: Wood.or Coal so. css nave aciwee cea aeane ewe ualeaina 330 3. Daily Weighing of Coal Used........................... 331 4., Cleaning the: Boiletieccwiaa we pea been i ee'see tees BS os & be 332 ov. Priming of BoilerSies4 4 s¢¢s9e¢ ga53 as ee eteas yao ea ee Eek 332 Gi “The: TMC ClO 4 chic Gnade aa eee an Wee adaetee eee 333 (, OMl-S6patahorss, ose .am geo eds ee P andes ode ites arg meee Hn .. 333 8. Belts, Pulley, and Speed Calculation..................... 334 APPENDIX. I. Lecat Stanparps ror Mitk—Dairy Laws......... ........ 335 II. Merric System oF WEIGHTS AND MEASURES WITH TABLES FOR CONVERTING THEM INTO CuSTOMARY UNITED States Equiv- ALENTS AND THE REVERSE......... 0.000 cee cece eee eee 336 BUTTER-MAKING., CHAPTER I. COMPOSITION OF MILK. Definition—Normal milk is a liquid secreted in special glands of all females belonging to the mammalian group. It is composed chiefly of water, proteids, fats, sugar, and minerals. Coloring-matters and gases and some organic acids are found in small quantities. All normal milk from the different classes of animals, such as mare, buffalo, goat, ewe, ass, and cow, has a general resem- blance in that it all contains water, fat, proteids, sugar, and ash. But milk from different animals varies in the relative proportions of its constituents. The chemical and_ physical properties are not alike. Human milk, when treated with half its volume of ammonium hydrate and the mixture kept at a temperature of 60° centigrade for about twenty minutes, assumes an intense red color. Cow’s milk turns faintly yellow if treated in the same way. ‘This test was reported by Unikoff, of St. Petersburg, at the meeting of the Medical Section, Royal Academy of Medicine, in Ireland. The various kinds of milk also differ from each other in their behavior towards rennet. Richmond has divided milk into two classes: Class T includes milk from the ewe, buffalo, goat, and cow. When rennet is added to the milk from these animals, the casein coagulates into a firm curd. Class IT includes human milk, milk of the ass, and mare. When rennet is added to the milk of these animals, a soft curd or none at all is formcd. The latter class seems 2 BUTTER-MAKING. to include the animals without horns, while the first includes those with horns. As the cow’s milk is used chiefly as a food, it has been subjected to more extended and more careful investigation than the milk of other animals, and, as a consequence, more definite knowledge has been obtained concerning its com- position, properties, and uses. The succeeding discussions have reference to cow's milk, if not otherwise stated. Composition of Milk.—It is impossible to get accurate figures on the composition of milk, as each of the milk con- stituents is subject to fluctuation from various conditions, such as individuality of cow, breed, season of the year, lacta- tion period, milking, and environment. The average composition, as determined by 200,000 analyses reported by Richmond as follows: WER Avis 6 aati eeaole inca a eee, “ko Pea bx backed Sears te Seu eee eae ont Oe O0) MilkssiPatiatveseseeieiertheceeswages “Ayo (OAREINIES shedcpcaheny Rabat Ged LO oe | Albian << AGAR a Gee Se at The composition of various kinds of milk is given by Konig as follows: No. of : Casein Milk- Specifi Analy. Water. Fat. ei cs sugar, | Ash. Gravity. Human... ...-. 107 87.41 | 3.78 2.29 6.21 .31 | 1.0270 Mare, as en se dae 50 90.78 | 1.21 1.99 5.67 .35 | 1.0347 Buffalo. ......... 8 82.25 | 7.51 5.05 4.44 .75 | 1.0350 ASSs cs wee Yew ales 7 89.64 | 1.64 222 5.99 .51 | 1.0345 COW a ieee eee 793 87.17 | 3.69 3.55 4.88 -71 | 1.0316 EWE: 6 dosh ios ans 2s 32 80.82 | 6.86 6.52 4.G1 .89 | 1.0341 GOabs gas. 8 peut vne 38 85.71 | 4.78 4.29 4.46 .76 | 1.0328 SOW? oa 3 aca sarang 8 84.04 | 4.55 7.23 3.23 | 1.05 | 1.038 Bitch, . .06 cess 28 75.44 | 9.57 | 11.17 3.09 .73 | 1.035 Elephant........ 3 79.30 | 9.10 2.51 8.59 .50 | 1.0313 Hippopotamus. . . 1 90.43 | 4.51] ...... 4.40 ll Camel. .......... 3 86.57 | 3.07 4 5.59 .77 | 1.042 Llama,......... 3 86.55 | 3.15 3.90 5.60 .80 | 1.034 COMPOSITION OF MILK. 3 Variation of Total Solids—As applied to milk, “ Total Solids,” is a term that includes fat, casein, albumen, sugar, and ash; in other words, all the milk constituents except the water. “Solids Not Fat” is a term often used, and includes the casein, albumen, sugar, and ash, or all the milk constituents except water and fat. “Serum” is a term used to designate all the milk constituents except the fat. The fat is the most valuable constituent of the total solids. The variation in the total solids of milk during the summer months is shown in the table quoted below from Dr. Van Slyke of Geneva, New York: Monit, at Water, ‘Total Solids, Mie nips or Ad 12.56 J UITIG <2, Ssceieer chee haeg ch Sa 87.31 12.69 Dilly; a geo sue ewaias 87.52 12.48 AUBUSte yo aa5 ery acs 87.37 12.63 September,....... 87 13 October, .......... 86.55 13.45 Dr. Van Slyke also studied the effect of the lactation period upon the total solids in milk. A herd of fifty cows, calving in different months of the year, was used in the experiment. The per cent of total solids of this herd seems to average a little high all through the ten months. The total solids were found to be 14° during the first month, decreasing to 13.47% during the next two months, then gradually increasing with the advance of the lactation period. In the tenth month the average total solids was 14.83%. Pingree, of Pennsylvania, reports having found normal milk from a cow, which contained 17.01% total solids. Sherman * reports a very high average total of the milk solids. He treated the milk from thirteen cows, and found it to contain on an average 18.03% of total solids. Ixnig reports a minimum of total solids of 9.31%, a maximum of 19.68%, and an average of 12.83%. The average total solids quoted above from Richmond is 12.90%, which agrees closely with Kénig’s results. * Journ. Am. Chem. Soc. 4 BUTITER-MAKING. The difference in total solids of milk from some ot the leading breeds has also been studied by Dr. Van Slyke. and the results are as follows: Per Cent Per Cent of Breed. of Water. ‘Total Solids. Holstein... ......- 88.20 11.80 Ayrshire... ...e.6- 87.25 12.75 Shorthorn... ...... 85.70 14.30 eV OMe sues es Kies 85.50 14.50 Guernsey........4. 85.10 14.90 Jersey, .ocsaee.aes 84.60 15.40 The maximum and minimum amounts of total solids men- tioned above are abnormal cases. The normal variations of the solids in milk are within comparatively narrow limits. For this reason the minimum standard for total milk solids, in states where dairy laws are in force, is fixed by law. Usually 12% is the minimum, Water.—From what has been said above concerning the total milk solids, it will be seen that water constitutes by far the largest portion of milk. It is quite uniform, and in milk from a mixed herd the water seldom falls below 86°% and seldom exceeds SS°(. Variations ranging from a little less than 80% to a trifle over 90% are on record. But such varia- tions must be looked upon as occurring in only a very few special cases. It has often been asserted that cows in the spring of the year, when they are pasturing on new grass, or feeding on other succulent foods, yield milk which contains an excess of water. Under such conditions there is a tendency for cows to pro- duce milk with a water content a trifle higher, as has already been shown by the figures quoted from Dr Van Slyke. As a rule this is much overestimated. It is even a common occur- rence to hear creamery operators say that their “soft” or “slushy ” butter, in the early spring, is due to the excess of the water present in the milk. This particular phase will be dis- cussed further under the heading of ‘‘ Fats in Milk.” The question has often been raisec Is the water in milk COMPOSITION OF MILK. 5 the same, or any more valuable than water obtained from other natural sources? The water in milk, so far as known, is transuded from the blood-vessels in the udder into the milk glands. It is so perfectly mixed with the other milk con- stituents, and holds the milk solids in such perfect emulsion and solution that it would seemingly be impossible to prepare milk so perfectly by artificial means. However, a substance is prepared by Jacob C. Van Marken, Neuweid, Germany, which, when added to water, produces a substance similar in appearance to watered skimmed milk. The preparation is named ‘Kalberrahm Vita.’’ The first name literally means calf-cream. It has a syrupy consistency, and in appearance resembles light-brownish molasses. It is sold in tin cans, and recommended highly for calf-feeding when mixed with skimmed milk. When mixed with water, it is recommended highly for hog-feeding. Water distilled from milk has the same appearance as ordi- nary distilled water. It is clear and colorless. The chemical reaction when phenolphthalein is used as an indicator, is neutral, the same as that of ordinary distilled water, even when dis- tilled from milk in which acid has developed. But there is a considerable difference in the taste and smell. This indi- cates that some of the volatile substances are distilled over with the water. The probability is that these flavoring substances are so closely associated with water in milk that they are in- separable, and that the only place where this water can be prepared so as to assume these qualities is in the cow’s udder, The conclusion would then be that the water in normal cow’s milk cannot be distilled and substituted again by natural water and the product retain its normal good flavor. Fat mw Minx. This is by far the most important constituent of milk, especially to creamery operators. It exists in the milk in sus- pension, in the form of globules so small as to be invisible to the naked eye. According to the best authorities, fat- 6 B UTTER-MAKING. globules, at ordinary living-room temperature, are present in milk in a liquid form. Cooling the milk to a very low tem- a. Skim milk, Ce) 058 ORS ° 5 08 2 O ° 70°25 eee C) 2Oo BOY O @, Colostrum, feo ee D5 8 Oo? & 6.2 ro) (°) Ove se ape,o © Gseor ene ree if Fic. 1—Microscopical appearance of different kinds of milk, 300 times, perature (about 50° F.) Magni (U_ 8, Farmers’ Bul. No, 42.) pened hardens them. When the globules are caused to unite, as in churning, they also solidify. The size of the fat-globules is very minute, and varies con- COMPOSITION OF MILK. 7 siderably, according to breeds, individual cows, and the stage in the lactation period. The globules in the milk from the same cow also vary a great deal. Lloyd found that fat-globules in Jersey milk to be from 8 to 12 micro-millimeters in diameter. Very few were less than 4 micro-millimeters (a micro-milli- meter is zj5y millimeter, or 3335; of an inch). The majority of the fat-globules in milk from Shorthorn cows measured from 6 to 8 micro-millimeters in diameter. According to Fleisch- mann, the size of fat-globules varies between 1.6 micro-milli- meters and 10 micro-millimeters in diameter. A Danish in- vestigator maintains that the diameter of fat-globules is between .0063 and .00014 millimeters, and that 1 cubic centi- meter of milk contains from 2.6 to 11.7 million globules. He also asserts that a reflection of the light renders it very difficult to get the proper size of the fat-globules, as the light tends to make the globules appear larger than they are in reality. It has been maintained by some that the larger fat-globules contain fats which are different from those contained in the smaller globules. But this is by some investigators considered to be a matter of conjecture. Most authorities now believe that there is no difference in the kinds of fat of the different- sized globules, even though some experiments * show that fat composed of larger globules has a finer flavor, and a little more oily appearance. From what has been said, it will be seen that the minute- ness of the fat-globules is almost inconceivable. They were first discovered in 1697 by A. von Leeuwenhoek. The minute state of division, or the form of emulsion in which they exist in milk, renders it easy to digest when consumed as a food. Properties of Fat.—The specific gravity of pure butter-fat at 15° centigrade is .93002. The refractive index of butter- fat at 22° centigrade is on an average 1.459. The melting- point of pure butter-fat, as now determined, varies between 32° and 37° centigrade. (90° F. and 99° F.) * Gembloux, Belgium, Creamery Jo., London, No. 8, Vol. I. 8 BUTTER-MAKING. When pure butter-tat 1s rapidly cooled, 1% solidifies into one solid mass; but if allowed to cool gradually, part of it solidifies, and part of it remains a liquid longer than other parts. This seems to indicate that some fats with a high melting-point separate out from the fats with a low melting-point. This behavior of pure butter-fat is not well understood, as it con- tradicts the now accepted theory that the different fats are in chemical combination with each other, rather than a me- chanical mixture of different glycerides of fat. Glycerides of Fat.—By this term we understand that the fatty acid radicals are in chemical combination with the glycerol] (glycerine) radical, thus: Fatty acid radicals. Glycerol radical. [ CysH7O2 (Butyric) CoH | CiallgsOs (Oleic) | CisH330» (Stearic) The chemical formula for glycerine is: Hydroxyl! groups, Glycerol radical. [ OH CsHs | OH | OH Comparing these two formulas, their difference and simi- larity are easily observed, and the reason why the term “ Gly- ceride of Fat” has been applied to such a compound is evident. Condition of Fat.—Whether the fats in milk exist in chem- ical combinaticn, or whether they exist as glyceride of butyrin, stearin, olein, ete., in the form of a mechanical mixture, is a question in dispute. If they exist in the latter form, the com- position of the different fats must be thus: Butyrin. Olein. Stearin, C4H702 | CigH3302 [ Ci sH3502 C3sHs {CaH7O2 C3Hs | CisH3s02 — CsHs | CigHs502 ete. | CsH702 | CigH3302 | Cre Ha 50s COMPOSITION OF MILK. 9 and the total fat made up of a mechanical mixture of these and the remainder of the fats in butter-fat. Richmond and other authors believe that fat probably exists in milk chemically, as first mentioned and illustrated; because, if the fat were a mixture of glycerine tributyrate with other elycerides of fat, butyrin or glycerol tributyrate could be dissolved out by the use of alcohol. But this is not the case. Moreover, if butyrin existed separately in milk, it would be possible to distill 1t off under reduced pressure. This cannot be done. Theory in Regard to Films Enveloping Fat-globules.—The extreme minuteness of the fat-globules in milk renders it almost impossible to determine by direct microscopical observation whether there is a membrane around each globule or not. Fleischmann and Lloyd assert that, so far as they were able to detect, there is no real membrane surrounding each globule. The theory generally accepted in the past was that the only film surrounding the fat-globules was simply due to sur- face tension, or to the fact that the molecules of the fat have a greater attraction for themselves than they have for the molecules of the serum, in which they are held in suspension. In support of this two thing: are considered: (1) The natural milk-fat may be removed from milk and artificial fat substituted in its place. The resultant milk has characteristics similar to milk containing normal fat; that is, the emulsion which milk forms with the artificial fat is ap- parently like that formed with the natural fat. (2) If there were a special albuminous membrane around each fat-globule, cream should contain a higher percentage of albuminoids than milk. This, Richmond maintains, ix not so. Dr. Storch concludes from extensive researches that there is a gelatinous membrane enveloping the fat-globules. His conelusions are based mainly upon the first three reasons given below. The other facts mentioned also support his conclusions: (1) When milk has been stained with ammoniacal picro- 10 BUTTER-MAKING carmine, and the cream washed with water until it is free from milk-sugar, a stained layer is present around each globule. (2) He has succeeded in isolating this gelatinous substance from cream and butter. Owing to its existence in these two substances, he assumes that it is also present in milk. (3) When ether is added to milk, the fat globules dissolve with difficulty, unless some alkali is added to the milk first. (4) Bichamp maintains that when ether is added to milk the fat-globules are enlarged due to the ether passing through the supposed membrane by the process of osmosis. He con- siders this fact sufficient to prove that there is a membrane encircling each globule. (5) Butter containing 85 to 86% fat is asserted by Rich- mond to have the same consistency as cream containing about 72% fat at the same temperature. The solidity of butter is due to the close proximity of the fat-globules. Now, if cream with less fat has the same consistency as butter, the proximity of the fat-globules must be equal to that of the butter; this would indicate that there is a membrane and that this membrane increases the size of the fat-globules. (6) The fact that cream separated by centrifugal force is more easily churned than cream of same richness separated by gravity methods, would also be explained if the fat glob- ules in milk had such a membrane surrounding them. This membrane, or what is believed to be a membrane, Storch has isolated and analyzed. He finds it to consist of 94°. of water and 6° of proteid. The reasons deduced by Storch are strong; and the behavior of cream and butter renders it probable that there is such a membrane enveloping each globule of fat. CLASSES OF Fats. There are two great classes or groups of fats present in the butter, namely: (1) Volatile and Soluble, (2) Non-volatile and Insoluble. COMPOSITION OF MILK. 11 It was previously stated that little is known concerning the way in which the fatty acids are combined with glycerine in the milk; but, for the sake of convenience, the fats will be referred to as if they exist as separate glycerides of fat. The terms “ Volatile” and ‘“ Non-volatile” are applied to the glycerides of fat, or to the fats as they exist in butter. Strictly speaking, this is not proper, as they do not assume the volatile characteristics until the glycerine separates from the fatty acids; it is only then that the latter becomes volatile. Volatile Fats.—The first group, or the volatile fats, include butyrin, caproin, caprylin, caprin, and laurin. Butyrin is the one present in the largest proportion. Laurin and caprin are partially non-volatile. Butyrin is the most important fat belonging to the volatile group. It is the most important quantitatively, and also qualitatively. So far as is known, butyrin is the least stable of any of the butter-fats. Under normal conditions, so long as the fatty acid remains in com- bination with the glycerol, it is not volatile nor soluble in water but as soon as separation takes place, due to the action of micro-organisms, or to the effect of light and air, then it becomes volatile, and escapes in the form of gas. According to the mass of evidence, these factors are the chief causes of rancidity in butter. It is also claimed that these volatile fats have the special properties of absorbing odors and gases to a greater extent than any of the other fats. This absorption takes place when fat comes into contact with the undesirable taints. For this reason it is essential that milk, cream, or butter be kept away from any foreign undesirable odors. These undesirable taints may also be imparted to the fat before the milk is drawn. If the cow is fed on undesirable food such as turnips, onions, garlic, ete., the milk from the cow assumes undesirable char- acteristic flavors, which can-easily be recognized in the finished product. On the other hand, such foods as well-cured sweet- clover hay, and bran, seem to impart desirable flavors to milk and butter. 12 BUTTER-MAKING. The presence of these volatile fats in butter is quite uniform, and is a distinguishing feature of pure butter-fat. The detec- tion of adulteration of butter with foreign fats is based chiefly upon the presence of these volatile fats. The characteristic desirable flavor of butter is also believed to be due to the pres- ence of the volatile fats. The volatile fats vary but slightly during the different seasons of the year. They are present in the greatest proportion during the spring and early summer months, when cows are fed on grass, and also during the early stage of the period of lactation. They decrease gradually as the lactation period advances. About 8% of the total fats in milk is volatile fats. Non-volatile Fats—This group constitutes about 92° of the total fats in butter. Chemists now agree that palmitin, stearin, olein, and myristin are the most important ones to be considered, as will be seen from the table quoted from Rich- mond. These non-volatile fats are of special importance, as the relative amount of each of these fats largely causes the varia- tion in the hardness and softness of the butter and butter-fat. The melting-point of these different fats varies according to the different investigators: olein is a liquid at ordinary tem- perature and melts at about 41° F.; stearin, on the other hand, has a melting-point of about 150° F.; palmitin also has a high melting-point, namely, about 142° F.; myristin melts at about 129° F. Olein has been found to be present in the greatest pro- portion during the spring, when cows are fed on grass. When cows are fed on normal dry food, as in the winter time, it is present in a much less degree. This, together with the small increase of volatile fats, is the cause of the softer butter so frequent in the spring. The hardness of the butter in the fall or winter is due chiefly to the presence of a slightly increased amount of the fats, with a high melting-point, as mentioned above. From what has been said above, one is led to believe that, COMPOSITION OF MILK. 13 by melting a sample of butter which contains these different fats, the fats with a low melting-point would melt first, and leave the remainder in an unmelted condition. Such is not the case. Butter-fat in this respect behaves a good deal like different metals with different fusing-points. When they are melted and mixed together, cooled and then remelted again, they assume a common melting-point. It is the same way with butter-fat. It melts at a temperature of 91° to 96° F. As the body temperature of cows (about 101° F.) is above this temperature, the fat globules are present in the milk in liquid form when milk is first drawn. melee en Average test . . oe, apeseA sass Cashni ae e ig) cat Beevers No. pounds butter-fat = ........ Hauling at... per 100Ibs ........ Price per pound a Bite eases Giese ac-ek Balance due you Be es & btst gt: Fy Gan ge. Sent hee liplabaeeedtry Total pounds milk delivered at creamery ee Ww es 8 wk Baeesecees Average test at creamery bee Celie Mean ep a Ed Stee eaienests Total pounds butter-fat at creamery & isin We “Rie Gte we | Me neelats f ———- -— Ibs.at ————. . 2. 2. Bo. eee | lanl : b eee ee Sales of butter j ree ae Seea oe $ Pee eee Less cts. for making. Balance due patrons. 2 1 ww wwe ww ww Bee eee eee Per cent overrun 2 be oly Legs) as fa. Spreng). ae el Gol Sesieho stances Testing witnessed by Prest Secy. At the end of the year a final statement should be made by the respective officers, similar to the following one: ANNUAL REPORT. Incorporated.......... 190... Commenced Operations,.......... 190... Hse er wede anh Annual Report, 190... of the CREAMERY COMPANY of ; , Iowa. ( Butter-maker; Asst. Butter-maker) CapiraL STock $............+. Pain IN $............., OFFICERS AND DIRECTORS. President, ————Secretary, ~———Treasurer. CREAMERY CALCULATION. SECRETARY’S REPORT. To the Stockholders: 115 Your Secretary herewith submits the following report for the year ending December 31, 190... Total pounds of milk received Total pounds butter-fat contained in same Total pounds butter manufactured Average test of butter-fat per hundred pounds of milk Average yield of butter per hundred pounds of milk. . . . . Average price paid per hundred pounds of milk . : Average price paid per hundred pounds of butter-fat Average per cent increase of churn over test (overrun) 4 F Average price received per pound of butter j Average monthly expenses of running creamery Average cost of manufacturing butter per pound. Following is a Monthly Statement for the year 190... January February March April May June. July. August . September October November . December . Totals STATEMENT OF CASH RECEIVED AND DISBURSED. REcEIPTS. Received for butter Total amount of cash re- ceived and paid to Treasurer Cash balance in hands of Treasurer, Jan. 190. . Total : DiIsBURSEMENTS, Paid to patrons for milk Running expenses of cream- ery and supplies on hand Paid for machinery, ma- terial, repairs, etc. (out of percentage fund) . Paid dividend on stock for 190. . (out of petoentags fi und) ; Paid dividend on stock for 190. . (out of percentage f und) Total amount of orders drawnon Treasurer . . Cash balance in hands of Treasurer, Jan. 190.. Total 116 BUTTER-MAKING. TREASURER’S REPORT. To the Stockholders of the Creamery Company: Your Treasurer herewith submits the following report: StaTEMENT OF CasH RECEIVED AND DISBURSED. RECEIPTS. DISBURSEMENTS. Total. © HR Total —eatiete a ieaat ine Respectfully submitted, , Treasurer. , Cashier of Bank. REPORT OF AUDITING COMMITTEE. To the Stockholders of the_ Creamery Company: We, the undersigned, appointed by your Board of Directors to examine and audit the Books, Accounts, and Vouchers of the Secretary and Treas- urer of the____ Creamery Company for the year 190..., hereby certify that we have carefully examined the same and compared them with the above reports of said officers, and find them correct. In witness whereof we have hereunto set our hands at , Iowa, this .... day of ...... A.D., 190.... ) | Auditing Committee. Paying for Fat in Cream Compared with Paying for Fat in Milk.—It is evident that when patrons deliver fat in the form of milk the creamery operator sustains a loss in the skimmed milk, while if the fat is delivered in the form of cream, no fat is lost in the skim-milk at the creamery, and consequently the cream patron should receive more per pound of fat delivered than the whole-milk patron, providing the quality of the fat in the cream is as good as that in the form of milk. The butter- maker should obtain a larger overrun from the fat of the cream than he does from the fat of the milk. The amount which the patrons should be paid for fat, delivered in the form of cream, depends upon the thoroughness of skimming. If 1000 pounds of milk testing 4% fat were bought and skimmed, there would be a loss of about .9 of a pound of fat during the skimming, which would make about 1 pound of butter, worth about 20 cents. If bought in the form of cream this loss would not be sustained. The above loss, during skimming, according to the figures mentioned, would amount to about half a cent CREAMERY CALCULATION. 117 per pound of butter manufactured. The fat lost during the skimming process would amount to about 2% of the total fat. If the cream fat be increased by 2%, an approximate basis for paying milk and cream patrons is obtained. Degree of Justice in Paying Cream Patrons More per Pound of Fat than the Milk Patrons.—There is another side to this question of reaching an equity of payment between the cream patrons and milk patrons. A cream patron should not receive more pay than a milk patron, unless the quality of the fat is as good as that delivered by the milk patron. It is a well- known fact that the fat delivered in the form of cream is, as a rule, and has been, much inferior to that delivered in the form of whole milk. This is evidently due to the fact that cream is not delivered daily to the creamery, and that it is improperly handled on the farm, and during transportation. According to the results obtained in the Iowa Educational Contest, and other scorings, butter from hand-separator cream on an average seldom scores above 90, on a scale of 100. It is safe to come to the conclusion that there is at least a difference of three points in quality in favor of creamery butter made from milk-fat. Mr. Healy, one of the best known butter judges, claims that in the near future butter will be sold more accord- ing to quality than it is now. He asserts that a fair basis of paying for butter according to scores would be to deduct a quarter of a cent for every point that the butter scores below 91, and an addition of a quarter of a cent for every point it scores above. This would make a difference of three-quarters of a cent per pound in the selling price of butter made from whole milk and that made from hand-separator cream. It was figured above that the loss from skimming would amount to about half a cent per pound of butter, thus leaving a margin of one-quarter of a cent in favor of the whole-milk patron per pound of butter, rather than being in favor of the cream patron. CHAPTER X. HEATING MILK PREVIOUS TO SKIMMING, Reasons for Heating.—Owing to the fact that all separators will skim closer and not clog so easily when milk is heated, nearly all creameries heat or warm the milk previous to skim- ming. By thus heating and stirring the milk in a pure atmo- sphere, many undesirable odors or taints escape. With an increase of temperature, the viscosity of the milk is lessened, due chiefly to the softening and separation of the fat-globules. Such an increased fluidity of the milk lessens the resistant force of the fat-globules when exposed to the centrifugal force of the separator. The higher the temperature the more fluid the milk becomes, and consequently the easier the fat can be separated. By warming the milk to a high temperature and leaving it for some time, and then cooling quickly again to skimming temperature (90° F.) and separating, the skimming efficiency of the separator is increased materially. If the milk has been standing at a very low teniperature for at least three hours, and then is quickly warmed up to the usual skimming tem- perature, and skimmed, the warming of the milk has com- paratively little effect in bringing it into a good condition for skimming. It will thus be seen that it is possible to skim milk at the same temperature, and yet get different results, due to previous temperature conditions. Duration of tem- perature should be considered as well as the temperature itself. The temperature to which milk should be heated previous to skimming varies according to different investigators. The temperature that has been mostly employed in the past in 118 HEATING MILK PREVIOUS TO SKIMMING. 119 this country, and perhaps at the present time, is about 90° F. This comparatively low temperature was fixed owing to the supposedly bad effect high skimming temperature had upon the body of the finished butter. Exposing milk, at high tem- peratures, to the centrifugal force in a separator was said to producea greasy body in butter. According to some ex- periments conducted at the Iowa Experiment Station by the authors during the year 1902, milk can be skimmed at 175° F. without any injury to the quality of the butter, providing the cream is cooled to ripening temperature, or below, as soon as it has been skimmed. After the ripening has been com- pleted the cream should be exposed at least three hours to a low temperature (50° F.) previous to churning. If the milk is heated in any of the best modern heaters, no injurious results to the quality of the butter will be obtained. Prof. Dean, at the Ontario Agricultural College, has also found it practical to heat to pasteurization temperature previous to. skimming. In many creameries in Denmark this method of heating milk is also followed. The Danes, as a rule, however, have the heated milk pass over a cooler before it goes into the separator. The chief difficulty encountered by the authors in heating milk to such a high temperature previous to skimming, was that the upper bearing in the separator got so hot that it was deemed injurious to the separator, although the bearing did not heat to such an extent as to cause the running of the machine to be abnormal in any way. Advantages of Warming Milk to High Heat Previous to Skimming.—The advantages of heating milk to a high tem- perature (175° F.) previous to skimming, may be summarized as follows: (1) Undesirable taints are eliminated from the milk to a greater extent than can be accomplished in any other way, without applying chemicals. (2) The heating of whole milk destroys the germs in the resultant skimmed milk and cream practically as efficiently OZT CR ‘Taye A, ye Araurvasg) ‘ALUIILIU JO quaWMOSUBIUIT poos vB Surasoys ‘wWool-1oyerrdoas BV JO louI0I W—L9 “SIT HEATING MILK PREVIOUS TO SKIMMING. 121 as when heated after the skimming process has been com- pleted. (3) Less heating and cooling apparatus is necessary. (4) Closer skimming. How Heated.—There are two methods by which milk is heated previous to skimming. Tirst, by the use of direct live steam; second, by the use of heaters which heat with steam or hot water indirectly. Fie. 68.—The Twentieth-century milk-heater. Heating of milk with direct live steam is accomplished in two ways: first, by entering a steam hose into the vat full of milk; and, second, by making use of special heaters, which allow steam to come in direct contact with the milk as the milk passes through. The method of heating milk with direct live steam cannot be too strongly condemned, because it leaves bad effects upon the flavor of the butter. At the Milwaukee National Butter contest in 1903, where over eight hundred exhibitors were represented, the authors noticed that where the criticism “burnt, oily flavor” was made on the score card, the milk from which the butter was made had in most cases been heated with live steam. The burnt flavor may possibly be due to the sudden excessive heat to which the milk will be exposed when coming in contact with live steam. The greatest danger, however, in heating milk with live steam is, that impurities from the pipes and boiler are likely to be transmitted to the 122 BUTTER-MAKING. milk, and cause bad flavors. In most of the creameries the exhaust-steam from the engine is used to heat the water for the boiler. This steam is likely to carry with it cylinder-oil, which will impart undesirable flavors to the butter. Some creameries are also using boiler compounds for the removal of scales. These, when subjected to high heat and pressure, are likely to be transmitted to the steam-pipes, and from there with the steam into the milk. The scale and rust of steam-pipes are also likely to be transferred to the milk. The right way to heat milk previous to skimming is to make use of one of the special heaters on the market, which heat by the use of steam or hot water indirectly. CHAPTER NI. SEPARATION OF CREAM. In the process of the manufacture of butter it is essential that the fat of the milk shall be concentrated into a compara- tively small portion of the milk-serum. This concentration of fat carries with it a portion of all the other milk constituents, and the product is called cream. It is possible to churn milk without any separation, but a much greater loss is attendant, if the fat is not brought together by the process called separa- tion. The different kinds of cream may be classified according to the different methods of cream-separating: ( Shallow-pan cream. Gravity cream... .. { Deep-setting cream. c | Water dilution cream (hydraulic). ream Hand-separator cream. Contriiigel ream { Creamery-separator cream. GRAVITY CREAMING. Shallow-pan System.—This method of creaming is used mostly on farms which are situated unfavorably in relation to a creamery, or for some other reasons do not send their milk to the creamery. It consists in placing the milk in shallow pans, from 2 to 4 inches in depth, as soon after milking as possible. The milk is then placed where it can be quickly cooled to a temperature of at least 60° F. A lower temperature than this is desirable if conditions permit. The atmosphere in the room in which the milk is standing must be pure, free from dust, 123 124 BUTTER-MAKING, draught, and any undesirable taints or odors, since it takes about thirty-six hours of quiet standing for the cream to rise. If there is a constant current of air in the room, a leathery cream is likely to form. At the end of this time the cream is removed by the use of a skimmer, made especially for this purpose. It is difficult, however, to remove all the cream by this means. If the conditions are such that cool water can be constantly circulated around the pans containing the milk, the tempera- ture can easily be made to go below 60° F., and the creaming process is facilitated. When such conditions are present, the depth of the milk in the pans can safely be increased to about 6 inches. Under the most favorable conditions about .5% fat will remain in the skimmed milk. Deep-setting System.—This system is undoubtedly the best method of gravity creaming When properly carried on the A fat can be removed so completely that no more than .2°, of fat remains in the skimmed milk. It consists of put- ting milk into deep cans (ordinary four- gallon shotgun cans are usually em- ployed) immediately after the milk has been drawn from the cow. Then it is put into cold water, and generally cooled down to, and maintained at, a Fig, 69.—Cooley creamer temperature of about 55° I’. The and elevator. i . F cream will rise in about twenty-four hours. Better results can be obtained if the water is cooled down to about 40° with the use of ice-water. One reason why this system is in use so much, even in creamery localities is that the cream obtained is nearly always of a good quality. The farmer knows that unless the milk be cooled quickly, and maintained at a low temperature, the cream will not rise freely. For this reason the milk is syste- matically and thoroughly cooled, which is one of the great essentials in order to check the growth of the ferments in milk SM ee = SEPARATION OF CREAM. 125 and keep the milk in good condition. In many parts of the eastern United States, the deep-setting system is in general use. A special form of can is used. The can is simply an ordinary four-gallon can, about 8 inches in diameter and 20 inches deep. It has a glass on one side near the bottom or near the top, which allows the reading of the thickness of the layer of cream. On each side of the glass is a graduated scale, which gives the reading in inches. In case the cream is being sold to a creamery, the hauler comes along, notes the depth of the layer of cream, and records the number of inches of cream opposite the patron’s name. At the end of the month, or whenever the time for payment comes, the money is appor- tioned according to the number of inches of cream delivered by each of the patrons. No test for fat is made. This is what is known as the ‘Cooley system,” and is used quite extensively in the East, especially in Massachusetts. While cream usually arrives at the creamery in a fair con- dition, there is the objection that the cream is always thin. It seldom contains any more than 18 or 20% of fat. No good explanation has yet been given why cream in a deep layer of milk at 40° F. should rise more quickly and more completely than in a thin layer at a higher temperature. * Arnold seeks to explain it by saying: “ Water is a better conductor of heat than fat; hence when the temperature of the milk varies either up or down, the water in the milk feels the effect of the heat or cold sooner than the fat in the cream does. Therefore the cream is always a little behind the water in swelling with heat or shrinking with cold, thus diminishing the difference between the specific gravity of the milk and cream when the temperature is rising, and increasing it when the temperature is falling.” This explanation is, according to Babcock,f not satisfactory. He says: ‘“‘ Though it is true that water is a better conductor of heat than fat, the small size of the fat-globules renders it * American Dairying, p. 210. 7 Wisconsin Experiment Station, Bull. 18, p. 24. 126 BUTTER-MAKING. impossible that under any circumstances there can be more than a small fraction of a degree of difference between the temperature of the fat and that of the milk serum. More- over, with the limits of temperature practical for a creamery, (90° to 40° F.), the coefficient of expansion of butter-fat is. more than three times as great as that of water, so that in order to maintain the same relative difference in their specific gravities when the temperature is falling, the milk serum must cool nearly three times as quickly as the fat. In other words, when the milk serum has cooled from 90° to 40°, or 50° F., the fat-glabules should have lost less than 17°, and should still have a temperature of over 70° F., a difference between the temperature of milk serum and fat of more than 33°. Such a condition is manifestly impossible, but no less difference than this would cause the fat to become relatively heavier than at first, and would operate against the creaming.” A low temperature increases the viscosity of the milk, and consequently it would seem that the resistant force of the fat-globules in their upward passage through the milk serum would be increased, and thus retard the creaming. Babcock maintains that fibrin is partially precipitated when milk is allowed to stand at a medium high temperature. The fibrin, when precipitated, forms a fine network of threads permeating the milk in all directions, similar to the network of fibrin in coagulated blood. It is possible to conceive that such a network would interfere with the rising of the fat-glob- ules, at comparatively high temperatures. The reason that fat-globules will rise more quickly and more completely in the deep-setting system than in the shallow-pan system, might be explained on this fibrin theory were it not for the fact that experiments conducted at the Cornell Experiment Station show that the setting and cooling of milk may be delayed long enough for this fibrin to form, without any effect upon the separation when set and cooled. Probable Explanation.—It is a well known fact in physics that most liquids, when present in the form of drops, increase SEPARATION OF CREAM. 127 their surface tension when the temperature is lowered. Owing to this increase in surface tension, the liquid drops unite together at a low temperature much more rapidly than they do at a high temperature. For instance, two drops of molten iron unite much more readily just previous to solidifying than they do while the temperature is higher, and the liquid more fluid. As the fat in milk is present in the form of small liquid globules, as mentioned previously, it seems probable that these fat-globules might have properties similar to those of the liquid mentioned above, and behave similarly in the milk, when set at low temperatures, in accordance with the deep setting method. If the fat-globules act in accordance with this theory, it seems probable that there is no real membrane, other than that resulting from surface tension, enveloping each fat-globule. If there were such a membrane, composed of albuminoid chiefly, then undoubtedly the fat-globules would not assume this property. With such a deep layer of milk the lower most fat-globules must evidently encounter a great many other globules as they rise. If the physical force mentioned does not facilitate the process of uniting the globules, they would partly unite without it. The more they unite in small bunches, or masses, the greater would be the tendency for them to rise, as explained previously, and more of the smaller fat-globules would be carried along. The bottom globules would tend to partly unite and form a filter, which passes up through the milk by the buoyant force, or force of levity. If this latter explanation holds true, then more of the milk constituents would be present in the cream from the deep- setting system than in the cream from the shallow-pan system. By comparing the cream raised by the shallow-pan system with that raised by the deep-setting system, before the cream has been removed from the milk, it will be noticed that the cream raised by the shallow-pan svstem appears to be much yellower than is that raised by the deep-setting system. This condition can only be due to the fact that the surface cream, 128 BUTTER-MAKING. raised by the shallow-pan system, contains more pure fat. The fat, as it rises, does not have the same opportunity of uniting with so many other globules, owing to the comparatively shallow layer it has to pass through, and the temperature is not low enough to facilitate the uniting of the globules; that is, providing the fat-globules act the same as most other liquids at lower temperatures. Water-dilution Cream (Hydraulic)—When milk is diluted with water, the fat or cream rises much more rapidly and completely to the surface than it would in its undiluted form. A creaming-can is based upon this principle, and it was expected to combine quickness, efficiency, and simplicity. The sepa- rator consists simply of a tin can into which the milk is poured and then diluted with cold water. In a few hours the cream rises to the surface. Arrangements are usually made so that the skim-milk can be drawn off from the bottom of the can. While the diluted form of the milk apparently causes the creaming to be more efficiently and quickly done, it can readily be seen that in order to have a skimming efficiency equal to other methods of skimming, it must leave only about half as much fat, because the milk is diluted with about an equal volume of water. If the water-diluted skimmed milk contains .2% fat, then the same skim-milk in the undiluted form would contain .4 per cent fat. The water-dilution method of skimming practically spoils skimmed milk for feeding purposes. Skimmed milk which contains a fourth or a half of water, has been robbed of its essential relish to the calf, and it becomes necessary for the calf to consume too much volume in order to get the required amount of nourishment. This water-dilution system also gives more volume to handle. If farm dairying were conducted on a large scale, the method would not be practicable. Another objection is that the cream which results from this dilution method is seldom of good quality. Most well- water contains a multitude of micro-organisms which, when SEPARATION OF CREAM, 129 added to the milk, produce putrefactive and undesirable results. Much well-water also is tainted to a greater or lesser degree. Especially is this so with water from shallow wells. Butter made from cream which has been diluted with water usually has a flattish poor flavor. The efficiency of separation of diluted and undiluted milk is reported by Wing * to be as follows: Diluted with 25% warm water set at 60° F. (39 trials), 0.77% fat in skim-milk; Undiluted, set at 60° F....... (30 trials), 1.00% fat in skim-milk Undiluted, set at 40° F....... (26 trials), 0.299% ‘* ‘ ee CENTRIFUGAL CREAMING. In the separation of cream by centrifugal machines, the same principle is used as in the gravity system of separation. The only difference is that in the centrifugal method the force which separates the cream from the milk is generated by artificial methods, and acts in a horizontal direction; in the gravity system the force which separates the cream from the milk is only that which results from the difference in the specific gravity of the cream and the skimmed milk, and the force acts in a vertical direction. The force generated in the sepa- rator is several hundred times greater than the natural force in the gravity method. For this reason the cream separates almost instantaneously after the milk has entered the separator and is exposed to the centrifugal force. Advantages.—The centrifugal separator has several advan- tages over the gravity method, which are apparent without detailed elaboration. In the first place, the range of tem- perature and condition of the milk at which the cream can be successfully separated is much greater than that for successful separation by the gravity method. Second, a much better quality of cream can be obtained by the centrifugal system, * Milk and Its Products, p. 105. 130 BUTTER-MAKING. as the separation can be done before the milk gets old, while by the gravity method the time required for efficient separation is so long that the cream deteriorates more or less before it is removed from the milk. Third, by the centrifugal method the thickness of the cream can be regulated to suit requirements, while by the gravity method the thickest cream that can be obtained is about 20%. Fourth, by the centrifugal method many impurities and undesirable germs are removed, while in the gravity method the exposure to open air more or less impure is likely to contaminate the milk with taints, and also allows the germs to fall into it. Fifth, by the centrifugal method the skimmed milk is left in an unadulterated condition. The milk can be skimmed soon after milking, or after it has been delivered to the creamery, and thus be in the best possible condition for feeding purposes. Sixth, the centrifugal method permits of a more thorough separation of the fat. Butter-fat, as a rule, is too expensive to feed, when good and much cheaper substitutes can be had. History of Centrifugal Separators——The first centrifugal separator was a very simple one. It consisted of buckets hanging on the ends of arms, or on the periphery of a rotating horizontal flat wheel which swung on a central axis. The milk was placed in the buckets and whirled for a time, and then the machine (if we may call it such) was stopped, and the cream removed in the same way as in the gravity system. This method of separation, according to J. H. Monrad,* had its origin in 1864. As early as 1859 Professor Fuchs of Carls- ruhe, Germany, suggested testing the richness of milk by swing- ing tubes holding the samples of milk. In 1864 Prandtl, a brewer of Munich, separated milk by such a device. In 1870 Rey. F. H. Bond, of Northport, Massachusetts, worked out a method of separation which consisted of two small glass jars attached to a spindle making 200 revolutions per minute. By one hour’s whirling the cream came to the top. * Dairy Messenger, Oct., 1892, p. 109. SEPARATION OF CREAM. 131 In 1875 Prandtl exhibited at Frankfort-on-the-Main a con- tinuous separator, which did not at the time attract much attention, due chiefly to the excessive amount of power needed to overcome the resistant force of the air. In 1876 a Danish engineer named Winstrup succeeded in improving the old bucket method. In 1877 Lefeldt and Lentch offered for sale four continuous separators with different capacities (from 110 to 600 pounds of milk per hour). During that year also the first practical centrifugal creamery was established at Kiel, Germany. In 1877 Houston and Thompson of Philadelphia filed a patent for the continuous method of separation of cream Fic. 70.—First centrifugal separator. (From Dairy Messenger.) from milk. The patent was allowed in 1891. In March, 1877, Lefeldt and Lentch invented a separator similar in construction to the hollow bowl—a more recent type. This machine did not revolve at so rapid a rate as our modern machines do, nor did it have arrangements for continuous inflow and discharge. It was intermittent in its work, and it was necessary to stop at intervals to remove the cream and skimmed milk. 1879 was the year which marked the greatest advancement toward the perfection of modern separators. The appearance of the Danish Weston, invented in Denmark, and the De Laval, in- vented in Sweden during that year, marked a great advance- 182 BUTTER-MAKING. ment. in the separation of cream from milk. This led to con- tinuous milk and cream discharges, and consequently also to the continuous inflow of whole milk. These machines were of the hollow-bowl construction. Modern Separators.—Since the year when the Danish Weston and the De Laval machines were invented, many different types of separators with different contrivances within the bowl have been put upon the market. Baron Bechtelsheim, of Munich, is given the credit of having discovered that certain Fic. 71.—The United States separator. contrivances on the inside of the machine increase the efficiency and capacity of skimming. This discovery was made, accord- ing to J. H. Monrad,* in 1890. This invention was bought by the De Laval Company. ,. The principal part of practically all the separators is a bowl rotating in a vertical position, with or without contrivances inside. the bowl. Machines having a bowl rotating in a hori- zontal position are, so far as the authors know, not in use at the present time. Such a machine was once manufactured at Hamburg, Germany, and was called ‘‘Peterson’s Centrifugal * Dairy Messenger, Jan. 1892, p. 9. SEPARATION OF CREAM. 133 Machine.” Another German machine, called ‘The Page,” was also manufactured in the horizontal bowl style. From the above it will be noticed that four separate steps are recognizable in the evolution and improvement of separators: 1. Revolving Bucket Centrifuge; 2. Intermittent Hollow Bow1; 3. Continuous Hollow Bowl; 4. Continuous Separator with contrivances within the Bowl. Fic. 72.—The Simplex separator. The science and practice of separation of milk and cream have seemingly reached a high state of efficiency. It seems almost improbable, considering the many new improved sepa- rators on the market that any other great improvement could be made which would add a separate stage to the improve- ment of our best centrifugal milk separators of to-day. Classification of Separators.—Owing to the many different standard types of separators now on the market, it is impossible to describe each one in detail. For this reason the classifi- 134 BUTTER-MAKING. cation appearing below has been made. There are undoubtedly many other types, especially in foreign countries, with which the writers are not familiar, and which are not mentioned here. The following classification will, in some measure, illustrate the different makes of separators on the market to-day: J De Laval (old style). Hollow bowl... | Sharples. Omega. Cause milk to | Empire. pass in thin } Davis. Farm sep- sheets vertical- | United States. arators. ly in bowl. National. | Reid. : Dairy Queen. nes De Laval Cause milk to | Peerless. separate into | | wea. almost hori-4{ Westphalia zontal thin | (Cleveland). i Se sheets. Towa. : Internat. Cream * Harvester. ( Improved Danish Weston (Reid). Hollow bowl | Sharples (old style). De Laval (old style). ror: Cause milk to | United States. sean pass in thin | Simplex. L tors. sheets _ verti- { Sharples (new cally in bowl. style). Contrivances in bowl. separate in al- | De Laval. | most horizon- | Springer. L tal sheets. 3 Cause milk P| Many of these separators which cause the milk to pass up and down in vertical sheets have the bowl contrivances corrugated, and perforated with holes so that the skim-milk and cream assume also a partly horizontal direction. Process of Separation.—From the illustrations, the structure of the more common types of separator bowls is readily understood. The whole milk may be made to enter at the bottom or top of the bowl when revolving. In the Sharples, the milk enters at the bottom. The more common way is to have the whole milk enter at the top. As the milk enters the bowl and is exposed to the centrifugal force, SEPARATION OF CREAM. 135 it immediately begins to separate into three distinct layers. The centrifugal force acting in a horizontal direction forces the heaviest portions of the milk and the precipitated albu- minoids, ash, filth, and a multitude of germs over next to Fic. 74.—The Sharples separator. the wall of the separator bowl, and into a solid and more or less gelatinous layer, which is known as the “ separator slime.” In very impure milk this substance is so plentiful that it is likely to clog the separator in a very short time, and before much separation is accomplished it is necessary to clean out the bowl. The second layer is the skim-milk, while the cream, being the lightest, is forced to the center of the bowl and forms the third portion mentioned. There is no distinct line of demarcation between the layers of skimmed milk and cream. They overlap each other and form a sort of zone, rather than a sharp separation. The richest cream is nearest the center of the bowl, and gets thinner toward the outer portion of the bowl; consequently, by turning the outlet for the cream, or cream-screw, nearer the center of the bowl, the cream is increased 136 BUTTER-MAKING. inrichness. Turning it away from the center causes the cream to be thinner. The skimmed milk that is forced clear to the circumference of the bowl contains the least fat, and con- sequently the skimmed milk is always first removed from this portion of the bowl. Usually the skim milk outlet is brought in towards the center of the bowl at one end through tubes extending from the circumference of the bowl. If this were not done, some difficulty would be involved in arranging a Fic. 75.—Showing “butter extractor” Fia. 76.—Showing cross-section of attached to De Laval separator. The De Laval separator bowl. butter extractor is not known to be in use now. receiving-pan for the discharged skim-milk. If the skim- milk were discharged near the circumference of the bowl, it would come out with a heavy force. Also, if the outlet for the skimmed milk were near the circumference of the bowl, a great deal more power would be required to run the machine. As the skimmed milk passes through the' tubes towards the center it gives up its force. The nearer the skimmed-milk outlet can be brought to the center of the bowl, the easier will the machine run. SEPARATION OF CREAM. 137 The size of the skimmed-milk outlet is usually made so that it bears a certain relation to the size of inlet, size of bowl, and to the speed of the machine. Most skimmed-milk outlets are mace so as to clischarge from .4 to about .9 or a little more, of the whole milk that enters the bowl. The remainder is the cream, which is forced to the center of the bowl and dis- charged through the cream outlet. Reuative AmMouNT aND RicHNESS OF MILK AND CREAM OBTAINED. The conditions which affect the relative amount of cream may be said to be as follows: 1. Regulation of the cream or skimmed-milk screw. 2. Rate of inflow to the bowl. 3. Speed of the machine. 4. Temperature of the milk. 1. Regulation of the Cream or Skimmed-milk Screw.—All modern machines, so far as known, have a device by which the relative amount of skimmed milk and cream can be con- trolled, and consequently the richness of the cream. Some machines have this device in the form of a cream-screw, and others as a skim-milk screw. The cream-screw in most of the machines has a hole on one side of it through which the cream is discharged. If this screw is turned so as to make the hole nearer the center, then the cream will be richer and less in quantity. If turned away from the center, then more and thinner cream will be discharged. In some machines there is a skim-milk screw which serves the same purpose. The method then of regulating the relative amount of cream and skimmed milk works in just the opposite direction; that is, when thicker cream and less of it is wanted, then the milk-screw is turned so as to bring the skimmed-milk outlet nearer the circumference of the bowl. This gives more skimmed milk and consequently less cream. If thinner and more cream is wanted, then the screw is turned in. This causes more milk to flow out through the cream outlet. The Reid hand separator 138 BUTTER-MAKING. is an example of this latter class. These two methods of regu- lating the thickness and amount of cream are the most common. It cannot be done while the machine is in motion. By some this is considered a drawback. Other separators have a device whereby the amount of cream can be regulated while the machine is in motion. For instance, on the improved Danish Weston, there is a screw attached to the skim-milk discharge-tube, by turning which the end or point of the tube can be made to be closer or farther away from the center, thus regulating the relative amount of cream and skimmed milk, and the thickness of the cream. 2. Rate of Inflow.—The rate of inflow of milk to the sepa- rator has a large influence on the relative amount of cream and skimmed milk. The greater the inflow to the separator, the more and thinner cream will be obtained, and with a dimin- ished inflow the less and thicker cream is obtained. This is due to the fact that at a given velocity of the machine the skim-milk discharge remains practically constant. So, if more milk is turned on, the only place where the discharge can increase is through the cream outlet; and if the inlet is diminished, the cream will diminish until a certain time, when the amount of milk, which runs into the machine, equals the amount discharged through the skim-milk outlet, and then there will be little or no cream. This is aptly illustrated by Wing: “If the milk is turned into the bowl at such a rate that .8 escapes through the skim-milk outlet, we shall have .8 skim-milk and .2 cream. If, now, we reduce the rate of inflow by .1, we shall get just as much skimmed milk as before, but only half as much cream; or, if the inflow is increased .1, we shall get the same amount of skimmed milk and one and a half times as much cream.” The completeness of sepa- ration will be the same so long as the separator is run within the range of its capacity. 3. Speed.—The speed of the separator influences the rela- tive amount of the cream and skimmed milk only in so far as an increase in the speed of the bowl increases the capacity SEPARATION OF CREAM. 139 of the skim-milk outlet, due to a more rapid discharge through the skim-milk outlet. The slower the bowl re- volves the less skimmed milk will be discharged, and conse- quently, if the inlet is constant, more and thinner cream will be the result. It should be stated in connection with this that the efficiency of skimming depends to a large extent upon the speed, and if attempts are made to increase the amount of cream and decrease the percentage of fat in it, by lowering the speed, an abnormal amount of fat will be left in the skimmed milk. 4. Temperature.—The temperature of milk usually does not influence the relative amount of milk and cream very much. The higher the temperature the more fluid the milk becomes, and consequently, all other conditions being the same, slightly more milk will run through at a high temperature than is the case with a lower temperature. This increase will show itself chiefly in the amount of cream, as the higher temperature has a greater relative effect upon the cream than it has upon the milk. By increasing the temperature of the milk, slightly more and thinner cream is obtained. ConpiTIons AFFECTING EFFICIENCY OF SEPARATORS. 1. Manner of Heating Milk.—Owing to the fact that fat- globules rapidly change their shape and property by exposing them to heat and excessive agitation, it is essential that care should be taken in heating milk previous to skimming. When fat-globules are heated they become more liquid, and if stirred very much the clusters of fat-globules break up more rapidly. The individual globules, if stirred violently, will break or sub- divide into several small ones. The higher the temperature of the milk, the more fluid the milk becomes, and the easier the separation. If milk is stirred violently, the individual fat- globules break up into smaller ones, which are separated from milk with difficulty. The following table * illustrates what * Hoard’s Dairyman, Fort Atkinson, Wis. 140 BUTTER-MAKING. effect the different degrees of agitation of milk has upon the efficiency of separation: Av. Fat No. of Per Cent Experi- in ments. Skim- milk. Milk heated in vat, not pumped................... 0000 eee 10. ~—«..117 Milk heated in Pasteurizer, 200 revolutions of agitator perminute 8 .115 oe im ims oe 250 ce oe ce ce ce 3 118 ce bc ce ce 300 oe ce oe oe ce 8 .134 a3 es oe “ce 350 ce “ce oe ce ce iy 143 “ec ce “ce ims 400 ce ce ce ce ce 7 .198 zs oe oe oc 500 ia ce oe ce ce 4 225 Milk pumped by the turbine pump at 122° F................ 3.129 ee i ote as ois BO OE GA Hirata ts 2g geet es 3 .119 ae ‘« with the pump, effective at 122°................ 3.117 we ENT alee a Oe GA ac sie sete ain se tg 3 115 In the above experiments the diameter of the agitator in the Pasteurizer was 14 inches. The speed at the periphery, at 250 revolutions per minute, was 5 feet per second. It will be seen from the above table that the higher the speed of the agitator, the greater the difficulty in getting a complete separation. Besides the speed of the agitator in the heating apparatus, undoubtedly the shape of the Pas- teurizer is a factor in determining the efficiency of the subsequent separation. For instance, the milk in most hori- zontal Pasteurizers is, even at low speed, exposed to con- siderable agitation. If the milk is suddenly heated from a low temperature to about 80° or 90° F. and then skimmed, the heating does not facilitate the skimming process very much. It is essential that the milk should be exposed to this temperature for a considerable time. The fat-globules do not warm as rapidly as the milk-serum. This diminishes the difference between the specific gravity of the two substances, consequently complete- ness of separation becomes more difficult. If milk is heated to a high temperature, say, for instance, 170° F., then the separation will be sufficiently complete without exposing the milk for any length of time to that temperature. SEPARATION OF CREAM. 141 Machines are now made, and are on the market, which will bring the milk, or the fat-globules in the milk, into such a condition that they cannot be separated from the milk. The process is called “homogenization.’’ It consists of bringing the milk under certain pressure, and then forcing it out through a special valve. This relief, through this special valve, causes the fat-globules to divide up into very minute ones. They divide up to such an extent that they cannot be separated from the milk by gravity methods, and it is impossible to get a complete separation by centrifugal methods. Homogeniza- tion of milk is carried on to some extent in Europe. The process practically insures uniform quality to the milk patrons in the distribution of milk in cities, and secures a more uniform consistency of the product. 2. Condition of the Milk.—In order to get complete separation, and keep the separator in good running order, it is essential that the milk should be in as good physical condition as possible. Coagulated, slimy, or otherwise viscous milk separates with difficulty. When such milk is on hand it should not be mixed with the milk that is in good condition, as it might tend to coag- ulate more of the good milk, and the coagulated or slimy lumps are likely to clog the separator. Such milk should be left until all the good milk has been separated. Then, if the coagu- lated or slimy milk is thoroughly stirred so as to reduce the lumpiness of it, it may be run through the separator success- fully. It is a good plan not to feed the separator quite so heavily when this quality of milk is being run through. By shutting off the inlet a little, it will usually run through without clogging. Milk containing impurities in suspension should be thoroughly strained previous to separation. Overfeeding the Separator—When a separator is being overfed with milk there is a tendency for the machine to do less complete work. This is due to the fact that the more milk is being fed into the separator the less time it will be exposed to the centrifugal force. It is impossible to underfeed the separator as well. As has been mentioned before, the 142 BUTTER-MAKING. inlet can be closed to such an extent as to cause nearly all the discharge to take place through the skim-milk tube. As a rule when the machine has been set so as to allow the milk to flow in at a certain rate, it will continue to admit prac- tically the same amount of milk all through the skimming period. Among the conditions which may alter the rate of inflow to some extent, are the amount of heat and the change of pressure, due to different amounts of milk in the receiving- vat. Temperature will slightly affect the rate of inflow. The higher the temperature, all other conditions being the same, the more milk will pass through the inlet. 3. Speed.—All modern machines have a device by which their speed can be determined. Most speed indicators consist of a little wheel, which, when pushed up against the spindle of the separator while running, turns around and permits the calcu- lation of the speed of the separator. If the wheel on the speed- indicator turns 10 revolutions during ten seconds, the machine would turn 1000 times during the same time. During one minute the separator will run six times as many revolutions, or 6000, as ten seconds is one-sixth of a minute. Most speed- indicators are so adjusted as to turn one revolution for every 100 revolutions of the machine. The higher the speed, the more thorough is the separation. Nearly all machines are balanced to do the best work at a certain definite speed, varying with different machines, and indicated in the directions for operating. It is essential that the machine should be brought up to speed gradually, and no milk be allowed to flow through it until after it has acquired its full speed. During the run, all machines are likely to vary more or less in speed, owing to different causes. Pulleys are likely to slip on the shaft, and belts are likely to become loose, and thus cause variations in the speed. The steam pressure is likely to get low, and cause all of the machinery in the creamery to run more slowly. This cause, however, is not a very common one where belt separators are used. If the engine has an auto- SEPARATION OF CREAM, 148 matic governor on it, the speed is usually quite uniform. Where steam-turbine machines are used, the speed of the machine is more likely to vary with the different amounts of steam pressure on the boiler. With turbine separators it is very essential to keep an even steam pressure. Some turbine separators have a safety-valve attached to prevent too high speed. The reason why the prevention of a variation in speed is so essential is that a slight variation in the speed has a compara- tively large effect upon reducing or increasing the centrifugal force. The centrifugal foree generated in a machine varies according to the diameter of the bowl, and according to the speed of the machine. The greater the diameter of the bowl, the less speed of velocity is required in order to get a certain force. The centrifugal force varies in direct proportion to the diameter of the bowl; that is, if the diameter of the bowl be doubled, then at the same speed, the centrifugal force has been doubled. The centrifugal force varies in quadratic proportion to the speed of the machine; that is, if the speed of the sepa- rator is doubled, the centrifugal force is increased four times. From this it will be seen that speed is a great factor in deter- mining the centrifugal force generated. It is not a good plan to have the diameter of the bowl too large, for the following reasons: A large bowl is more likely to be thrown out of balance; it is harder to keep on the bearings; and it is heavier and more unhandy to handle. For these reasons it is better to lessen the diameter of the bowl and increase the speed. This, of course, is true only to a certain limit. Steadiness in Running.—Smooth running of a separator is one of the first essentials. If a machine runs roughly, there will not be good separation, and it is dangerous to run it. The bowl itself is likely to jump out, or burst. The causes for unsteadiness in running are many. It may be due to a bent or sprung spindle; the machine not standing level; changing covers to bowls; using clamps which do not fit the bowl cover; unclean, worn-out bearings; condition of the bowl, and con- trivances inside the bowl; and dented and rusty bowls. Occa- 144 BUTTER-MAKING. sionally it happens that a machine is run backwards. This is likely to cause the cover of the bowl to run off. Thickness of Cream.—The efficiency of skimming depends to some extent upon the thickness of the cream skimmed. Most separators, however, will skim within quite a wide range as to thickness. The richness of cream usually skimmed by separators is about from 25% to 50%. Most separators, how- ever, will do good skimming even if the cream contains as high as 60% fat. This, however, should be considered to be about the maximum, in order to get the best results from a separator. Slush in Bowl.—As has been mentioned before, there is always a thick, slimy substance which adheres to the bowl- wall. The composition of separator-slime is, according to Fleischmann, as follows: VWVISTET ok Pile ea ated Goce ails canine aren 67.3 ENG ne Bei Pe Rear ea Da ah Oh fad nd de 1.1 Caseous matter.......... .............. 25.9 Other organic substances. . 2.1 Ash. ... 3.6 100.0 At the center of the bowl, or along the axis which runs perpendicular in the bowl, there is always considerable cream. It is practically impossible to get all the cream out of the bowl, even if it is flushed with much water. The amount of slush varies somewhat with the different kinds of separators. For this reason, it is essential that it should be taken into con- sideration when the comparative efficiency of skimming of different separators is considered. When the test extends over a comparatively long period, and the milk skimmed amounts to several thousand pounds, then the bowl-slush does not affect the conditions for comparative results very much; but when the test is short, and only a hundred pounds of milk, or a similar amount, is skimmed, then the amount of fat left in the bowl- slush will have considerable influence upon deciding which one is the most efficient machine. SEPARATION OF CREAM. 145 General Remarks.—In order to keep the separator in good running order, it must receive care. The belt should not be too tight, nor too loose. If too tight it is likely to bind, heat, and set the bearings of the separator. If too loose it is likely to slp, and to wear out more quickly. The machine should be well oiled. It is better to use a trifle too much oil than not enough. If a bearing is once heated, the machine will never run as well again. The bowl should be handled with great care. Bowls, or parts belonging to the bowl, can be kept from rusting by boiling them in water, or by steaming them thoroughly after they have been cleaned. If scalding-hot water is used before the milky portion has been washed off, the albuminoids will be scalded on to such a degree that it is difficult to get them off. This applies to all dairy and creamery utensils. Hot water is said to be best in which to dip tin or iron-ware after washing in order to keep them from rusting. If the bowl, pail, or whatever utensil it may be, is turned over to drain after being dipped in hot water, the heat taken up by the utensil will in a short time perfectly dry the apparatus. If the bowl is steamed, it should be heated thoroughly to make it dry quickly. If the milk supply gets short during the run, and it is neces- sary to run the machine without feeding milk, then the machine should always be flushed with luke-warm water. This will, in a measure, prevent clogging. Scalding-hot water should never be used for flushing the separator. The cream and skimmed- milk tubes should be carefully cleaned, with the special wire provided for that purpose, each time the machine is washed. The contrivances on the inside of the bowl should also be handled with care so as not to injure them in any way. They should be treated with hot water, as mentioned above, in order to keep them from rusting. When the bowl is not to be used for some time, it should be oiled well so as to prevent it from rusting. It is easier to oil a separator bowl than it is to scour the rust off later on. CHAPTER XII. FARM SEPARATORS. Tue conditions affecting the efficiency of skimming and the relative amount of cream and skim-milk described under “Creamery Separation’ apply to farm separators as well. The conditions under which the farm separators are operated war- rant a few separate remarks on this subject. Introduction of Farm Separators——Small, or hand, separa- tors, have been manufactured for a good many years. It is, however, not until comparatively recent years that they have been numerous enough to be of commercial importance. The people in the Central West (Iowa, Kansas, Nebraska, Missouri, Minnesota, and Illinois) have been most prominent in intro- ducing farm separators. In the year 1894 hand separators were introduced in Iowa, but it was not until 1898 that they gained sufficient foothold to be of commercial importance. According to the Iowa Dairy Commissioner’s report of 1898, there were then only 904 farm separators in the state of Iowa. Now, in 1904, there are more than 17,000 separators. Glancing over the statistics it will be seen that the rate of increase in hand separators during the years intervening between 1898 and 1904 has been uniform and rapid. This proves that the dairy business is still in a transitional period, and the intro- duction of hand separators still on the increase. Such a time in any industry is always accompanied by more or less incon- venience, difficulty, and dissatisfaction. To receive a part of the butter-fat in the form of cream, and the other part in the form of milk, is undesirable. Under such a system it is always difficult to get milk or cream routes organized; proper sampling 146 FARM SEPARATORS. 147 becomes more or less difficult, and the quality of butter is harder to control. Reasons for Introducing Farm Separators.—It requires an investment of about $100 to purchase a hand separator. Fie. 77.—The Omega hand separator. Most of the butter made from hand-separator cream is of poor quality. Still, in the face of this, separators have rapidly -u creased. It may be concluded that there must be some good reasons why farmers are continuing to invest in farm separators. There are undoubtedly many reasons why farmers prefer hand 148 BUTTER-MAKING. separators; reasons which are, to a large extent, confined to local conditions. Only a few of the chief and general reasons can be given here: (1) The farmer is able to skim the milk at once after it has been drawn, thereby enabling him to feed the milk while i AT aye Fic. 78.—The Iowa hand separator. Fic. 79——The De Laval hand separator (Baby No. 1). it is in a warm, sweet, unadulterated condition. If he hauled the milk to the creamery, the skimmed milk would be likely to come back in a sour and curdled condition, and at times watery. (In a well-conducted creamery these latter conditions do not exist.) (2) The high cost of hauling in many instances makes it almost impossible to get the milk to the creamery. Even if the roads are good, the distance to the creamery is frequently so great that it is impossible to get haulers, nor is it practical for every farmer to haul his own milk every day. Especially is this so during the busy season of the year. In the fall, when milk is scarce, it is almost impossible for the hauler to FARM SEPARATORS. 149 get enough milk to make it profitable. In many cases it is necessary to pay an excessive price for hauling milk. When cream routes are established instead of milk routes, one hauler can usually cover as much territory as three could Fie. 80.—Sinayilone hand separator and the different parts of bowl. under the milk system. Two thousand pounds of milk, testing 4% and containing 80 pounds of fat, would represent approx- imately a load of milk. At 12 cents per 100 pounds, this would mean a cost of $2.40 for getting that much milk 150 BUTTER-MAKING. hauled. If the same amount of butter-fat were hauled in the form of cream, it could be gathered for about 14 cents per pound of fat, or the cost of hauling in this particular case would be $1.20. Under the milk system it would be neces- sary to haul the milk to the creamery every day, while under the cream system it is usually gathered every other day in the summer, and every three days in the winter. It is usually considered that there is a saving of about 14 to 2 Fig. 81.—Sharples separator and parts of bowl. cents per pound of butter-fat in hauling, by making use of the cream system instead of the milk system. This, of course, would vary according to local conditions. 3. The use of hand-separators makes farmers more inde- pendent than they are under the whole-milk system. They are not compelled to support their local creamery unless they deemit advisable. They can ship their cream to any place that they may choose. If the butter from the hand-separator cream is going to be of as good quality as that made by the whole- milk system, the cream should be delivered as often as possible. Every day is preferable to every other day. In case frequent FARM SEPARATORS. 15k delivery is made, then it becomes quite essential for the farmer to patronize the local creamery, as very few farmers keep suffi- cient cows to get enough cream to pay them to ship by rail i i Hl eu Fria. 82.—The National hand separator and parts of bowl. every day. Usually it does not cost much more to ship a can full of cream than it does to ship it half or three-quarters full. 152 BUTTER-MAKING. Objections to Farm Separators.—Under the present manner of carrying on the hand-separator system, the quality of butter manufactured from the cream shipped into the central plants is much poorer than that made from whole milk. This is not due to ) ony fault of the system, but to the poor care which the separator and cream receive. The sepa- rator on the farm is frequently kept in an unsuitable place. Often it is located in the barn. If the milk is separated in such a place it will absorb odors and undesirable taints. The cream is seldom taken care of properly after it is separated. The separators often are not cleaned well. A separator can- not be kept in good condition by simply flushing out the bowl] with cold water at the end of each separation. It must be taken Fic. 83.—De Laval apart at the close of each skimming; have all hand separator. the parts washed thoroughly in luke-warm water, and then scalded. The time and power it requires to skim the milk and to care for the milk is in many instances considered objectionable to the system. Thickness of Cream.—The thickness of cream which most butter-makers at central plants prefer is cream containing about 30 to 40% of fat. Such cream is not thick enough to cause any inconvenience in sampling and weighing. It can be diluted with a good starter and ripened without getting it so thin as to produce unfavorable conditions for churning. By some it is deemed advisable to skim even thicker than this, up to 50°¢. Cream containing this much fat, however, is difficult to handle especially in winter, during cold weather. It gets so stiff that it is difficult to pour, and there is also danger of losing more or less cream through its adhering to the sides of the cans. A thick cream is advisable from the farmer’s standpoint. The thicker the cream is, the more skim-milk he will retain on the farm for feeding purposes. It can also readily be seen FARM SEPARATORS. 153 that if thin cream is skimmed greater can capacity is necessary, and the express charges will be heavier than if the thicker cream were skimmed. Rich cream does not sour so rapidly as does thin cream. | im a | | | il Fic. 85.—Empire hand separator. The thickness of cream can be readily ascertained by the use of a Babcock test, which every farmer should have in his possession. A whole outfit for testing fat in cream or milk 154 BUTTER-MAKING. can be had for about $8.00 from any creamery supply-house. By the use of such a test, the farmer can test his cream and Fic. 86.—Peerless hand separator and cross-section of bowl. skimmed milk. He can also test the milk of each individual cow in the herd, thereby ascertaining which ones are profitable. Fic. 87.—Agos hand tester. By the use of such a test on the farm, the farmer can test his cream daily, and compare results with those from the creamery, FARM SEPARATORS. 155 thereby enabling him to detect any mistake which may happen at the creamery. Power for Farm Separators.—Hand-power is often men- Fig. 88.—The Dairy Queen hand separator. Fie. 89.—Scales. tioned as an objection to farm separators. When a considerable quantity of milk is to be skimmed, it is certainly hard work to skim with hand-power. Windmills could not well be used i oe wer Fig. 90.—Tread-power attached to United States hand separator. as they do not give uniform speed. The power must be steady and uniform. Farm separators are often run with tread- power. This kind of power is very applicable, and does not cost 156 BUTTER-MAKING. ig igi _ —) 20% 25% 30 % 40% Fic. 91.—Showing the height to which cream free from air-bubbles must be raised in a pipette to get 18 grams of cream. It shows that to measure cream in a pipette is inaccurate in cream testing. (lowa State Dairy Com. Report, 1903.) FARM SEPARATORS. 157 anything after the tread-power has once been purchased. The power can be supplied by using different kinds of animals. Fic. 92.—Showing how the internal bowl devices of Westphalia hand sepa- rator are washed. (N. Y. Produce Review and American Creamery.) Sheep, goats, dogs, and bulls are used for this purpose. The process usually does not last very long, and it is not considered heavy work. Steam is good power, but it is hardly ever obtainable on the farm. Small gasoline-engines are also used very successfully. The machine should always run smoothly in order to get efficient skimming. It should never be stopped and started with a jerk. Start it slowly and there will be less dan- ger of breaking any of the gearing parts. The bowl and inside parts should be kept from rusting as described previously on page 145. The bearings should be well oiled. It is a good plan to have an extra Fic. 93.—Davis hand separator. bearing or two on hand, so that if one happens to wear 158 BUTTER-MAKING. out another one can be put in. The bearings should be cleaned at intervals. When kerosene is occasionally used on the hearings they do not need to be cleaned so often, because Fie. 94.—Dairy utensils in the battered condition of the can on left and with tin off in many places inside, cannot be kept clean and should be discarded. (Kansas State Board of Agriculture Report No. 87, 1903.) it keeps them from gumming. The machine should be turned at the proper speed, as indicated in the directions. A thicker cream will result from rapid turning; consequently more skimmed milk will be obtained. Slow turning causes ineffi- cient skimming and thinner cream. Care of Cream on the Farm.—The first step in the produc- tion of good cream is clean milking. This can only be accom- plished when barn, cows, and utensils are clean. It is a good 6¢T CTI ‘FS ‘INel) “Bury a1ojoq sieppn saoo Suruvoy; 160 BUTTER-MAKING. plan to dampen a cloth, and wipe off the cow’s udder and sides each time previous to milking. The milker should never wet his hands while milking. Dust should not be stirred up in the barn during milking, as the dust particles carry with them a large number of undesirable germs. When these settle in milk they are likely to produce taints. If cloth, strainers are used they should be kept scrupulously clean. It is advis- able not to use them at all, as good sanitary wire-gauze strainers are inexpensive. Progeny ofa single germ in © twelve hours Fig. 95.—Showing the effect of cooling milk on the growth of bacteria. The beneficial results of early chilling are readily apparent. (From Bul. 62, Wis.) If these conditions are complied with, and the separator is kept in a good clean condition, the milk will have compara- tively few germs in it. Some germs, however, will enter the milk, and in order to keep them from developing, it is essential to cool the cream or milk immediately. Low temperature retards and practically prevents the development of germ life. It is a well-known fact that when milk is kept cool, it will remain sweet much longer than if kept at a high temperature. Never mix two milkings or skimmings unless both are well cooled first. In order to cool cream quickly, it should be stirred during cooling. The ordinary four-gallon shot-gun cans are good and suitable for keeping milk and cream. They have a large cooling surface in proportion to their cubical content. FARM SEPARATORS. 161 The milk or cream should be cooled as low as the water will cool it. It is well to cool it even lower than this if ice is ob- tainable. In keeping milk, the temperature should never go Fic. 97.—The condition of the cow shown in this cut is favorable for the accumulation of loose dirt. (Bul. 84, III.) above 60° F. Cooling to 50° F., if it can be accomplished, is much more desirable for keeping milk or cream in good condi- tion. 162 BUTTER-MAKING. If considerable milk is handled, it is well to provide a milk- house. it should be built large enough to contain the sepa- rator, water-tank, and other utensils necessary for home butter- Fig. 98.—A clean cow. The dirt cannot adhere to this cow to so great an extent as to the one shown in Fig. 97. (Bul. 84, Ill.) making, such as a churn and butter-worker. There should be plenty of windows on all sides to give good ventilation. The water-tank should be connected directly with the well, so that ae) 5 = a as do Be ae) ae 3 o OG ae ov Ei Q, Zz a a = o “5 a ab ansas State Board of Agricult des whitewashed, well 1 i si (Report of I Cement, floor, iron stalls, hown in Fig. 100. xterior s y barn. Fig. 99.—A sanitary dair system of ventilation. E 162 FOL uo “SOGT LS “ON ‘aMyMoLUSY JO prvog 97819 sesuevyy jo ysodexy) “66 ‘BLT ut ; : “qysua ee arian ‘ye, uo uorjzod ur sopg ‘ureq Anrep deayo Apearyereduioas ‘yeou Y—OOT ‘PI UMOYS JOLIOJUT rnd eScomiat f COL CIIE ‘26 ING) ‘sdaputd Jo sorpOUT NTS TIT pataAod ‘pred popvis-[Jam ‘uve W— TOL “PIT % pees z pees io ners oS 991 CTI ‘26 Ing) ‘oyeTNUMo0e 03 PAMOL[E st oMeeur ay} tonpa ut pre paprasun u~— TOL “DLT FARM SEPARATORS. 167 the water can be pumped directly to the tank holding the milk and cream. From this place the water can be run out into the stock-tank. This arrangement allows the milk to be kept at the lowest possible temperature. It is Just as essential to cool the milk during the winter as it is during the summer. By pumping water through this tank practically all the time, the water in the tank will be kept from freezing. It is well to keep the surface of the water higher Fie. 103.—The average weight of dirt which falls from muddy udders dur- ing milking is ninety times as great as that which falls from the same udder after washing, and when udders are slightly soiled it is twenty- two times as great. (Bul. 84, Ill.) than the surface of the milk in the can. This will prevent the milk from freezing so easily. If the cold is too severe, a tank- heater can easily be secured which will moderate the tem- perature a trifle. Disposition of the Cream.—There are two ways of disposing of cream on the farm: (1) selling it to creameries or other parties, and (2) making it into butter on the farm. The former method is usually the most advantageous. Creameries, as a rule, are better equipped to control the quality of butter. The price per pound of butter-fat is usually about 2 cents below “New York Extras.” A few of the best co-operative cream- eries are able to pay more than that. 168 Ill.) it (Bul. 9 vilway station. Fie. 104.—Milk- and cream-cans at the r FARM SEPARATORS. 169 Shipping of Cream.—If cream is sent or shipped to cream- eries and central plants, it is essential that it be delivered as frequently as possible, and that it be delivered in cans which will help keep it in good condition. If cream is to be shipped any great distance and be exposed to the sun, it is advisable to use special jacketed cans, which retard the transmission of heat. It is a good plan to cover the cans with a wet sack ve cloth during the summer, and the use of a dry sack on Fic. 105.—The Buhl milk and cream can. Fig. 106.—A barrel churn. the outside in the winter often prevents the cream from freezing. Making Butteron the Farm.—If cream is kept in good condition and proper skill is applied, the best of butter can be made on the farm. Theoretically, better butter can be made on the farm than at the creamery, because all conditions can be controlled better. This is not so in creameries. One can of bad cream mixed with a quantity of good cream is likely to contaminate and injure the whole lot. The cream which is to be made into butter on the farm should be ripened, or soured, properly before it is churned. In creameries, starters 170 BUTTER-MAKING. are used to set up a quick and desirable fermentation in the cream. Conditions are usually such on the farm that it is not (a> Fig. 107.—The Davis swing-churn., Fie. 108.—Sanitary glass milk- bottle and cap for same. convenient and practical to use a starter. In the summer the cream can be lifted out of the cold water the morning previous Fic. 109.—Skinner butter-worker. to churning, and it will sour during the day. In the evening, or when it has soured, it can be set back into the water to cool. The next morning it is ready for churning. In the winter the creain can be soured by warming it up or keeping it in a warm place. If some good sour milk is on hand, it might be added, FARM SEPARATORS. 171 and the cream will sour much quicker. It is very essential that the cream can be cooled to a low temperature (50° I.) and left Fic. 111.—The Cherry jacketed cream can. I 1 5 | ne 4 pue Joqjo ur Quid #08 os} == UPI ¢ 20781, BF, 08 > o a rm “MED, FESISIOL 8 %,B |] : fan) qa» ~>S a ee et o {== =| o 2s Be ano 8 oo 4 OW As the specific it would take 168,000 pounds of ice per year. heat of cream is only about 0.7, the final amount needed for cooling the cream would be only 117,600 pounds, or about 59 tons. COOLING FACILITIES FOR CREAMERIES., 319 The next consideration is the ice needed for cooling the butter. Roughly speaking, there will be about 600 pounds of butter. Suppose the butter needs to be cooled 30° F. Granting that the specific heat of butter is the same as that of water, it would require 30 pounds of ice to cool 142 pounds of butter 30° F. There will therefore be needed daily 126 pounds of ice for cooling the butter. As the specific heat of butter is only about 0.4, 51 pounds of ice are necessary daily. For eight months 12,240 pounds will be needed. The amount of ice needed in a refrigerator above that needed for cooling the butter cannot be calculated. We may count on 25% radia- tion and 25% as an allowance for cooling tubs and packages. The total ice needed for cooling the butter will then be 24,480 pounds, or about 123 tons. Counting on 20% loss incidental to transportation and melting in the ice-house, 89 tons of ice are needed for cooling the cream and butter the number of degrees mentioned above. One cubic foot of ice at 32° F. weighs 57.5 pounds. If 1 cubic foot of ice weighs 57.5 pounds, 89 tons would occupy a space equal to 3093 cubic feet, and would require an ice- house of dimensions approximately as follows: 16 ft. high, 14 ft. wide, and 14 ft. long. These dimensions are given only as examples. The height, width, and length may need to be changed to conform with local conditions. One thing should be kept in mind, it is always better to have an ice-house a little too large rather than too small. Filling the Ice-house.—The chief objects to be sought in packing icc into an icehouse already properly constructed, are: first, to exclude circulation of air through the mass of ice and thus prevent melting; second, to pack it in such a manner that it can easily be removed in whole blocks; third, to pack it with such material that it will leave the ice as clean as is consistent with other important sought objects. The packing material which is most commonly used in the central western States is sawdust. This is very efficient in excluding air, lasting, and usually cheap, but soils the ice, 320 BUTTER-MAKING. so that considerable water needs to be used with which to rinse it. As a consequence of this latter, considerable ice is wasted. Straw is used successfully. It leaves the ice much cleaner, but is not so effective in preserving the ice. Shavings are good, but as a rule are too expensive and not available. Some use no packing material other than ice and snow. When the blocks of ice are put into the ice-house, they are packed closely together. A man with a hatchet chips the block of ice in such a way as to fit them snugly together. The small cracks are filled with fine ice and snow. The experience of the authors is that, by this method, the blocks of ice are likely to solidly freeze together, so the ice cannot be removed without break- ing it up into irregular pieces. This is hard work, and con- siderable ice is wasted. Another method of filling ice-houses in successful use is that of running a small layer of water into the building and allowing it to freeze. The doors in the ice-house are opened during a protractive period of cold weather. The bottom of the ice-house is covered with building-paper. Water is run on top of this and allowed to freeze until a layer of ice about a foot in thickness has been obtained. Then another layer of paper is made to cover the ice and more water flooded on and frozen. This process is continued until the ice-house is filled. The paper between the layers prevents the ice from freezing into one solid mass, and facilitates the removal of the ice. When the ice is stored in an insulated house, combined with the refrigerator, no packing material is used except on the top of the ice. Shavings are good to pile on the top of ice when the ice-house has been filled. They are clean and effective in preserving the ice. The cost of filling an ice-house with natural ice, obtainable within a distance of about eight miles, will vary in different localities, but may be said to range between $0.60 and $1.25 per ton. The creamery furnishes a man to pack it into the ic2-house. COOLING FACILITIES FOR CREAMERIES., 321 Source of Ice.—The ice for creamery use should be ob- tained from as pure water as possible. A large running stream is always better than a small polluted stream. Usually the creamery can codperate with butchers, restaurants, hotel- men, and other local ice-users in building a dam in a suitable stream. The ice can also as a rule be harvested cheaper by cooperation. Some creameries have constructed ice-ponds near the icc- house. If there is a clay or impervious bottom, this works successfully and economically. The pond is filled and kept filled from the creamery water-supply or from a tile drain inlet. Care should be taken not to use stagnant water and water in which weeds and other rubbish have been allowed to accu- mulate. The pond should be deep enough so that the water will not freeze to the bottom and produce dirty ice. The pond should also be filled with water to overflowing when freezing is begun, otherwise slush and snow are likely to accumulate together with dust from the fields and roads, producing impure ice. The ice is best when frozen from the top down. A hole is bored and kept open in the ice during the freezing process. Through this opening the pond is supplied with water as rapidly as it subsides. When the water is solidly up against the bottom of the ice it will show in the opening or hole in the ice. To construct an ice-pond on gravelly soil is useless, and to pack such a pond with a sufficiently thick layer of clay to pre- vent leakage of water is under most conditions, impracticable. Usace or Ice in CooLtinc CREAM. 1. Directly. 2. Indirectly. 1. The cooling of cream in creameries by putting ice directly into the cream has been much practiced in the past. The method is yet used considerably, especially where the old open vats are still in use. Some of these open vats are jacketed 322 BUTTER-MAKING., and some are not. Cream in unjacketed vats could not well be cooled in any other way than by using ice directly in the cream and stirring until cold. To keep cold any length of time, considerable excess of ice needs to be used. Such a method of cooling cream has its advantages as well as disadvantages. The latter, however, clearly outweighs the former. The advantages are that the cream can be cooled in a very short time, and it does not require any special investment for up-to-date ripening-vats, nor special machinery for the purpose of pumping the cooling medium. The chief disadvantages are: First, impurities and un- desirable germs are liable to be introduced, which would injure the quality of the cream and otherwise work harm to the quality and keeping property of the butter; second, the melt- ing of the ice would dilute the cream. This would render the cream less sour, impart a marked flat, insipid taste to the cream and butter, and produce more buttermilk which, if it contained a certain per cent fat, would mean a greater loss of fat during the churning process. The use of ice directly in the cream for cooling purposes should not be resorted to unless it is necessary. With the best quality of cream this method is still more unsatisfactory, as it greatly lowers the quality of butter. With cream in very poor condition previous to ripening, the chances for lowering the quality of butter are not so ereat. 2. The cooling of cream with ice indirectly is by far the best method. With the use of our up-to-date ripening-vats, the cooling of cream is an easy matter. But where the creamery is already in possession of a good open vat and the manage- ment not disposed to discard it to install a new one, the ques- tion is different. Some open vats have a jacket and special open space at one end for holding crushed ice. These vats will control and hold temperature better than those with just a jacket around. The cooling of cream on a large scale by circulating ice-water COOLING FACILITIES FOR CREAMERIES, 323 through the jacket, at best, is a slow process. Usually too slow to be effective and practical. This cooling process is carried out by mixing the ice and water together in a separate vat to which a rotary pump is attached, forcing the water through the jacket and again returned to the ice and water-tank to be cooled. The slow- ness of this cooling process can in a measure be overcome by mixing salt with the ice and water. This will cause the ice to melt faster, and consequently cool the brine to a lower degree of temperature than was possible to obtain with water and ice. In case it is desirable, a set of coils can be made which will fit into the open vat. The inlet and outlet of these coils can be connected up by means of rubber hose with the pipes con- veying the brine to and from the ripener. The coils can be made to move up and down, by means of a rope attached to and leading from the coils through a pulley near the loft and fastened to a small crank at the end of a shaft. When the shaft turns the crank will also turn and cause the coils in the vat to move up and down. In the absence of a special up-to- date ripener, this manner of cooling works very satisfactorily. A butter refrigerator containing a tank, as already de- scribed, could be cooled by pumping brine through it in similar manner, as described for cream cooling, except that no coils are needed. MECHANICAL REFRIGERATION. Application of in Creameries.—Mechanical refrigeration has been considered expensive and impracticable on a small scale until within a few years. The science of producing cold arti- ficially has been simplified and reduced to such a practical basis that it is now used in many large as well as smaller plants where formerly natural ice was used altogether. Where at least 10,000 pounds of milk, or its equivalent in cream, are received daily during the summer months, mechanical refrigeration is considered practicable. 324 BUTTER-MAKING, On another page a table of comparative cost of natural ice and mechanical refrigeration is given. It was also stated in that connection that the cost of mechanical refrigeration would vary under different conditions. The chief factors affecting the cost of mechanical refrigeration may be said to be similar to those affecting the economic running of the re- maining machinery, such as kind of fuel used, skill of fireman, style and condition of boiler, proportion of boiler power to work done, upon the correlative size of all machinery, upon kind of insulation and care of cooling-rooms, and upon efh- ciency of compressor and whole refrigerating system. Chemicals Used for Mechanical Refrigeration—The most common substances used in mechanical refrigeration are am- monia and carbonic acid. A number of others are in use, but from a creamery standpoint, these only are of importance. Ammonia is used chiefly. It is efficient, cheap, and not so dangerous to life and property as are some of the others. Anhydrous ammonia has a boiling-point of 27° below zero at atmospheric pressure. The latent heat of ammonia is also great. Ammonia has great chemical stability, and is not explosive in nature. Ammonia attacks copper and_ brass, but has no effect upon iron and steel pipes. If ammonia should escape through a leak into a room, the operator can protect himself from the effects of the gas by breathing through a wet sponge held in the mouth. Ammonia leaks may be detected by holding a glass rod dipped in hydrochloric acid to the place where the leak may be. When ammonia comes in contact with hydrochloric acid, white fumes are formed. Carbonic acid is used considerably in Europe, and is chiefly favored because the gas is not highly poisonous; in case of leak it does not spoil contents of refrigerator, and it liquefies at a high temperature (90° to 100° F.), and is therefore favored in tropical climes. Principles of Producing Cold Artificially.—The chief principle involved in producing artificial cold is that when a substance passes from a liquid into a gaseous state, a definite amount of COOLING FACILITIES FOR CREAMERIES. 325: latent heat is absorbed. When water in a kettle on the stove begins to boil and passes off into steam, no higher temperature can be reached. No matter how much heat is applied under those same conditions, the temperature remains the same. This extra heat is used in transforming the water into steam. If this steam were confined, and that heat removed, by cooling, the steam would again pass into a liquid state. We are familiar with the coolness produced by rapid evaporation of perspira- tion from the body. Mechanical refrigeration is virtually a process of evaporation of the cooling media, during which heat is absorbed and liquefaction of the cooling medium by compression and cooling to remove that absorbed heat. To increase the ability of the cooling medium to absorb heat it is compressed and liquefied. So we might say that any com- pression refrigerating system has three separate operations necessary to form the complete cycle of mechanical refrigeration, viz.: 1. Compression of the ammonia gas. 2. Condensation of the ammonia gas. 3. Expansion of the ammonia gas. 1. The machine which causes the compression of the am- monia gas is called the compressor. In construction it is much like a steam-engine. Small machines are single, but large machines are double acting. Gas is drawn in, on the suction stroke, compressed and discharged on the return stroke. The pressure generated varies between 120 and 175 pounds per square inch. During the compression heat is developed in proportion to pressure exerted. The greater the pressure the higher the temperature of the gas. Part of the heat of com- pression is carried off by means of a continuous stream of water running through a jacket around the cylinder. 2. From the compressor the gas is forced through the pipes into the condensing coils, in which the warm compressed gas is cooled still more. When sufficient heat has been removed from this gas, it assumes a liquid condition and is ready to expand into a gaseous form for the purpose of absorbing heat. 326 BUTTER-MAKING. and producing cold. During the cooling and condensing pro- cesses each pound of ammonia parts with about 560 units of heat, which amount can again be absorbed when it expands into gas at the lower pressure. 3. This liquefied gas, which is still under great pressure, is then admitted through what is termed the expansion-valve. This valve is especially constructed for that purpose, and has only a very minute opening in it for the admission of the liquid ammonia. On the expansion side the pressure is low (20 to 30 lbs.). As the liquid ammonia emerges from the high- pressure side through the expansion-valve into the expansion side, it forms a gas. This expanded gas may then be circulated through coils for cooling purposes. From there it passes back into the suction side of the compressor ready to go through another similar cycle. From the above description it will be seen that there are two sides to the system, the expansion side and the compression side. The compression side extends from the compressor to the expansion-valve; the expansion side from the expansion- valve to the suction side of the compressor, inclusive. Transferring the Cold.—The methods of transferring the cold to the different places in the building vary. There are two systems, viz.: 1. Direct Expansion. °. Brine System. 1. By the direct-expansion system the condensing-pipes of the system are extended to the room or place at which the cooling is to be done. An extended set of expansion coils then convey the gas which absorbs the heat. A lower temperature can be produced by this method than with the brine system. 2. In the brine system a large brine-tank is placed some- where in the creamery at a place most convenient with respect to cooling. This tank contains a strong solution of brine. The chief reason why brine is used in preference to water is that brine has a very low freezing-point. This will vary with different degrees of saturation. COOLING FACILITIES FOR CREAMERIES, 327 Either one, sodium chloride (common salt), or calcium chloride, may be used for brine. The latter is considered best chiefly because it is not so hard on the pipes and it keeps the brine pipes cleaner than does a salt brine. give properties of brine made from these two substances. SHowInG Properties oF SOLUTION OF SALT. (Chloride of Sodium.) The tables (SIEBLY). Pounds H ecific F ‘ : a Bale by] Salt er, |Beloretcr| por Gallgn Gravity at] Spgcitic | Freezing: | Freesing Weight. | Gallon of | at go? F. | at aa" F.| 38) F. : Fahr. | Ceisius. olution. 4°C. 1 0.084 4 8.40 1.007 0.992 30.5 -— 0.8 2 0.169 8 8.46 1.015 0.984 29.3 -—- 1.5 2.5 0.212 10 8.50 1.019 0.980 28.6 - 1.9 3 0.256 12 8.53 1.023 0.976 27.8 — 2.3 3.5 0.300 14 8.56 1.026 0.972 27.1 — 2.7 4 0.344 16 8.59 1.030 0.968 26.6 — 3.0 5 0.433 20 8.65 1.037 0.960 25.2 — 3.8 6 0.523 24 8.72 1.045 0.946 23.9 — 4.5 7 0.617 28 8.78 1.053 0.932 22.5 — 5.3 8 0.708 32 8.85 1.061 0.919 21.2 — 6.0 9 0.802 36 8.91 1.068 0.905 19.9 — 6.7 10 0.897 40 8.97 1.076 0.892 18.7 — 7.4 12 1.092 48 9.10 1.091 0.874 16.0 — 8.9 15 1.389 60 9.26 1.115 0.855 12.2 —11.0 20 1.928 80 9.64 1.155 0.829 6.1 —14.4 24 2.376 96 9.90 1.187 0.795 2 -17.1 25 2.488 100 9.97 1.196 0.783 0.5 —17.8 26 2.610 104 10.04 1.204 0.771 -1.1 —18.4 PROPERTIES OF SOLUTION oF CHLORIDE OF CALCIUM. (SIEBLY). PeWelane,” | Specific Heat. | Sree Grane” [in Dearees Fane, | in Degrees Cale, 1 0.996 1.009 31 — 0.5 5 0.964 1.043 27.5 — 2.5 10 0.896 1.087 22 ee 15 0.860 1.134 15 — 9.6 20 0.834 1.182 5 —14.8 25 0.790 1.234 -8 =22.1 The expansion-coils pass through the brine-tank and cool Special pumps force the cold brine through pipes to the cream vat, cooling coils, ice-cream freezer, etc. the brine. 328 BUTTER MAKING. For creameries the brine system is the only practical sys- tem. It is preferred because, first, cold can be stored in an insulated brine-tank and used at will without running the com- pressor. In case of a prolonged stoppage due to some accident a brine made by a mixture of ice-water and salt could be temporarily substituted; second, less ammonia is required to charge the system; third, fewer couplings and less ammonia pipes are necessary. This latter would decrease the danger of ammonia leakage and cost of pipes. CHAPTER XNII. ECONOMIC OPERATION OF CREAMERY. INASMUCH as it is impossible within the limited space in this work to take up a detailed discussion of the various principles and practices of operating boilers, engines, mechanical re- frigerators, and other creamery machinery, only a few of the chief factors common to creamery practice and effecting the economic operation shall here be discussed. For more com- plete information students are referred to works treating specially of these phases. Firing the Boiler—Much fuel can be wasted and saved ac- cording to the completeness with which the combustion occurs. This again depends upon the manner of firing, upon the regu- lation of the draught, and upon the kind of boiler. The fire on the grates should never be too thick nor should too much coal be loaded on the fire at any one time. A thin, even fire permits of a more complete combustion than when clinkers and cinders are allowed to accumulate on bottom of fire, and a heap of unburned coal on top. By this latter method of firing, the grates are likely to be injured. To get the most heat from the coal the draught should be regulated. The combustible part of the coal is of two kinds: first, the fixed carbon, and second, the volatile matter. The former is the coke or the part of coal which is seen on the grates as a mass of glowing fire. The latter consists of the gases which pass off when a certain temperature is reached, and which, when mixed with a certain amount of air at a given tem- perature, will burn. The heavy black trail of smoke seen rising B29 330 BUTTER-M AKING, from chimneys is partially wasted coal. If the grates are choked with a thick fire, no air can pass through, and the volatile parts of coal pass off without being burned. Burning Wood or Coal.—In some localities this question is of minor importance, as conditions may be such that coal only can be used. In other sections, where both are obtain- able, it is of great importance. The following table* shows figures obtained at five factories in Wisconsin where soft coal was burned and five others where wood was used. DariLty Fur, Usep at SEVERAL CREAMERIES. Pounds of Milk Pounds of Cost of Coal |Estimated Cost perBey | Beach | per "Tea” | per Bay.” 3500 500 $3.55 $0.90 8000 400 3.00 0.60 23000 1000 4.05 2.00 6000 300 3.50 0.50 5300 500 3.15 0.80 P Is of Milk 7 ; “Skimmer ' cen a mee Price per Cord. ee per Day. . 2000 t $1.25 $0.32 3400 + 2.25 0.37 6500 4 1.25 0.32 3800 + 2.25 j 0.37 4500 4 1.80 0.60 These are the best obtainable figures of comparison under creamery conditions. In connection with burning wood the dryness of it is an important consideration. If the wood is wet its power of producing heat is greatly lessened. A certain amount of heat is used in evaporating the water in the wood. Air-dry wood will contain from 12% to 25% water. The quality of coal is another variable factor. In general, and from table below, it might be said that 24 pounds of wood are equal to one pound of lump coal. * Farrington in Hoard’s Dairyman. ECONOMIC OPERATION OF CREAMERY. 331 The following comparative table is given by Kent: Hickory or hard maple, weight per cord 4500 lbs. = 1800 to 2000 lbs. of coal. White oak oe SE 8 BBbO He = 1640 to ITS Poplar, chestnut and cedar ‘‘ ‘‘ ‘‘ 2350 ‘‘ = 940 to 1050 ‘‘ ‘‘ ‘° Pine ee ee 2000 §* = 800 to 925 ff Ss fF Whether a creamery can economically use slack or lump coal is another question worth considering. Slack coal is used very little in local creameries, first, because it is more difficult to use in firing. Usually help is scarce, and coal which requires less attention in firing than slack, is preferred. Second, slack coal is subject to spontaneous combustion and likely to set buildings afire. Some, if not all insurance companies, dis- criminate against creameries using slack coal as fuel. Third, special grates (rocking grates) are essential to get best results from using slack. Fourth, slack coal is dirty and the dust from it will lodge all over in the boiler and engine room. Slack coal, where conditions are at all favorable for its use, is, as a rule, cheap to burn. According to experimental data, 1 pound of slack coal will produce about 4 pounds of steam, and 1 pound of lump coal will produce about 6 pounds of steam. The price of the two will vary, but usually the rela- tion is, slack coal, $1.25 per ton; lump coal, $3.25 per ton. If 1 pound of lump coal produces 6 pounds of steam, a ton will produce 12,000 pounds. If 1 pound of slack coal produces 4 pounds of steam, to produce 12,000 pounds will require 2992 pounds of slack coal, which would cost $1.87. The difference in producing 12,000 pounds of steam in favor of slack coal would then be $1.38. Daily Weighing of Coal Used.—The advantage of daily weighing of coal used in creameries cannot be too strongly emphasized. That business phase of creamery work has been much neglected in the past. If the coal used daily is not weighed, a serious loss or leak may continue without detec- tion. Firing the boiler is a daily occurrence, and if a small loss occurs, the total loss at the end of the year would cut short the profits. 332 BUTTER-MAKING. The weighing can conveniently be done by fitting a box similar to an enlarged flat-sided curd pail in shape on a pair of platform scales. After the scale and box have been pur- chased there are nc additional expenses and very little extra labor required. Cleaning the Boiler—The amount of coal used will vary with several factors, viz.: cleanliness of flues, sediment in the boiler, condition of fire, kind of boiler, steam leaks, pipe in- sulation, etc. The two first factors are frequently neglected. The flues should be cleaned every morning before the day’s run. The inside of the boiler should be kept clean. Heavy scale on the inside of the boiler and flues, and heavy sedi- ments on the bottom of the boiler, should never be allowed to accumulate. Some water naturally contains a large amount of minerals and leaves a heavy deposit in the boiler. The oper- ator should learn to know the condition of the water, and the frequency of cleaning the inside of the boiler be governed accordingly. One cleaning per month is sufficient with most water. In some instances, one cleaning per week is necessary. The collection of scale and sediment within the boiler affect the economic operation in at least three ways: First, more fucl is needed; second, the boiler itself is likely to warp; third, foaming or priming of the boiler is likely to occur. If scale clings to the flues when washed, it may be removed by putting some sal-soda and water into the boiler and boil for several hours. Some use a boiler compound for preventing scales. This is not necessary, nor to be recommended except in extreme cases of mineral water. The boiler should be frequently blown off at low pressure. Priming of Boilers.—When considerable water passes over with the steam the boiler is said to be priming. This water in the steam interferes with the running of the engine. So much water in the steam fills the engine-cylinder and results in broken piston or cylinder-head. The engine jerks and thumps to such an extent that there is danger of breaking other parts of the machinery. ECONOMIC OPERATION OF CREAMERY. 333 The foaming or priming of boilers is due chiefly to: . Too much water in the boiler. . Working the boiler beyond its capacity. . Allowing mud and minerals to accumulate in boiler. . Using too much of certain boiler compounds. . Some water naturally contains a large percentage of certain minerals which are conducive to foaming. The Injector.—The injector on the boiler frequently causes the operator some annoyance by refusing to work. The common causes of this are: 1. Too low boiler steam pressure. 2. Steam obtained from a pipe already supplying steam for other purposes. 3. Leaks in suction pipe due to shortage of supply pipe or holes in pipe. 4. Too hot supply water. 5. Seale in injector, preventing proper working of valves. 6. Steam containing too much water. Oil-separators.—Considerable saving can be accomplished in a creamery if the exhaust steam is utilized. This steam may be used for pasteurizing the skim-milk, for heating the milk previous to separation, for heating the creamery, and for heat- ing the water for the boiler. The exhaust steam contains considerable oil and should be purified before it is used for any other purposes. Several forms of these steam purifiers are on the market. They are simple, inexpensive, and can be attached to the exhaust-pipe of any engine. All steam and water pipes should be carefully drained in the winter to prevent freezing. Belts, Pulley and Speed Calculation.—The length of a belt may best be determined by measuring over the two pulleys with a tape or a string. To calculate the size of a drive pulley when the speed of it is known, the diameter of the driver pulley is multiplied by its speed, the product divided by the speed of the driven aor wd 334 BUTTER-MAKING. pulley, the quotient will be the diameter or size of the needed pulley. To calculate the speed of a driven pulley, multiply the diameter by the speed of the driver pulley and divide the product by the diameter of the driven pulley; the quotient is the speed or number of revolutions per minute. APPENDIX. LEGAL STANDARDS FOR MILK—DAIRY LAWS.* The following States and Territories, viz., Alabama, Arizona, Arkansas, California, Colorado, Delaware, Florida, Louisiana, Mississippi, Missouri, Montana, North Dakota, Texas, and Wyoming, have established no legal standard. The Dominion of Canada, Connecticut, Idaho, Illinois, Indiana, Kansas, Kentucky, Maryland, Nebraska, Nevada, New Mexico, North Carolina, Oklahoma, South Dakota, Ten- nessee, Utah, Virginia, and West Virginia have general laws prohibiting dilution, skimming, or other adulteration. In other States the percentage standards are as follows: Specific Total Gravity. Solids. Fats. Per Cent. District of Columbia. ................00000 cece ee eee 12.5 3.5 GEOR IA odd ahd ats crces cit tees Hee vece Aisle osaliains urea aeeetenetes 12 3.5 LOW Bie far 6 HemtaRangue Site Gaede Ee AAU eects Rann ie RR cd Os 12.5 3 Main Ge caeeMee rea honest waite uit oh Uae: «pay Be dah et 12 3 Massachusetts (Apr. to Aug., inclusive)..... ........... 12 3 re (Sept. to Mar. Oe Nett tee egeeoRes 13 3.7 Michigans 236.03 cetnd centtet an Cee a wear aels 1.029-1.033 12.5 3 Minnesota: ¢ cesses Geter ke eee eee guy ee a Ween sak Se 13 3.5 New Hamipshire:. sonc.csce oda eh heten ade adauededad 13 IN GW CPSC Yai friacarh c iaintns aon! and. ovat oe dup nein ee aS aveee ae 12 New York: savcctcot ante tap degorecrieieet, AtereeSeaey 12 3 Ohio (May and June)...............00..02 cece eee eee 11.5 vats ‘« (July to April, inclusive)... ...........0 ......0000, 12 3 OremOn es aioe ache eee cA Sea aie MU LR ee Oeics Bok 12 3 Pennsylvania: tiv sccnswiau a eas ce ude ekee 1.029-1.033 12.5 3 Rhode: Wsland)..20 yjcceeet tug acneeiete eens ae ceadaeane 12 2.5 South: Carolinas so: sec0 c.g deka niede Beno Mage hee way 11.5 3 Vermont (May and June)... ..........000. cee eee eee 12 a (July to April, inclusive). ......... 0 .......00.. 12.5 ae Washingtones scccc tac peu witinn pidemten ole dada ees 11 3 Wistonsines< coca ones oreo eee Seen Gh yesadohag sae 3 * From Wing in “ Milk and Its Products.” + Applies only to cities of the second and third classes. 335 336 METRIC SYSTEM. METRIC SYSTEM.* METRIC SYSTEM OF WEIGHTS AND MEASURES AND TABLES FOR THE CONVERSION OF METRIC WEIGHTS AND MEAS- URES INTO CUSTOMARY UNITED STATES EQUIVALENTS AND THE REVERSE. In the metric system the meter is the base of all the weiglit= and measures which it employs. The meter was intended to be, and is very nearly, one t:n- millionth part of the distance measured on a meridian of th: earth from the equator to the pole, and equals about 39.37 inches or nearly 3 feet 32 inches. The meter is the primary unit of length. Upon the meter are based the following primary units: the square meter, the are, the cubic meter or stere, the liter, and the gram. The square meter is the unit of measure for small surfaces ; as the surface of a floor, table, ete. The are is the unit of land measure; this is a square whose side is 10 meters in length, and which contains 100 square meters. The cubic meter or stere is the unit of volume; this is a cube whose edge is 1 meter in length. The liter is the unit of capacity; this is the capacity of a cube whose edge is one-tenth of a meter in length. The gram is the unit of weight; this is the weight of dis- tilled water contained in a cube whose edge is the one-hundredth part of a meter; a gram is therefore the one-thousandth part of a kilogram, and the one-millionth part of a metric ton. * From The American Chamber of Commerce, APPENDIX. 337 Measures or LENGTH. Metric Denominations and Values. Equivalents in Denominations in Use. Myriameter........ 10,000 meters 6.2137 miles Kilometer......... 1,000 meters .62137 mile, or 3,280 ft. 10 in. Hectometer........ 100 meters 328 feet 1 inch Dekameter........ 10 meters 393.7 inches Meter............. 1 meter 39.37 inches Decimeter......... .1 meter 3.937 inches Centimeter........ .01 meter .3937 inch Millimeter. ........ .001 meter .0394 inch MEASURES OF SURFACE. Metric Denominations and Values. Equivalents in Denominations in Use. Hectare. .......... 10,000 square meters 2.471 acres ATO dct b oe dgsen 100 square meters 119.6 square yards Centare........... 1 square meter 1,550 square inches MeaAsuRES oF CaPACITY. Metric Denominations and Values. Equivalents in Denominations in Use. Names. ee Cubic Measure. Dry Measure. Tactaiel or tvie pes \ 1,000 1 cubic meter 1.308 cu. yds. 264.17 gals. Hectoliter. 100 .1 cubie meter 2 bush. 3.35 pks.| 26.417 gals. Dekaliter. 10 10 cu. decimeters | 9.08 quarts 2.6417 gals. Liter. ...... 1 1 cu. decimeter .908 quart 1.0567 qts. Deciliter.... Jl 1 cu. decimeter | 6.1022 cu. ins. 845 gill Centiliter. .. .01 | 10 cu. centimeters | .6102 cu. in. 338 fl. oz. Milliliter.... .001| 1 cu. centimeter .661 cu. in. .27 fl.dram 338 METRIC SYSTEM. WEIGHTS. Metric Denominations and Values. pe err at al Weight of What Names. Number of Quanity of Water at |Avoirdupois Weight. e Maximum Density. Metric ton......... 1,000,000 1 cubic meter 2204.6 pounds Quintal........... 100,000 1 hectoliter 220.46 pounds Myriagram........ 10,000 1 dekaliter 22.046 pounds Kilogram or kilo. .. . 1,000 1 liter 2.2046 pounds Hectogram. ..... 100 1 deciliter 3.5274 ounces Dekagram......... 10 10 cubic centimeters .8527 ounce Gram. ............ 1 1 cubic centimeter 15.432 grains Decigram......... 1 .1 cubic centimeter 1.5432 grains Centigram......... .01 | 10 cubic millimeters 1543 grain Milligram.......... .001 | 1 cubic millimeter .0154 grain CoMMON MEASURES AND WSIGHTS, WITH THEIR METRIC EQUIVALENTS. The following are some of the Measures in common use, with their equiva- lents in measures of the Metric System: Monee: Equivalents. Common Measures. Equivalents. 1 inch 2.54 centimeters 1 cord 3.624 steres 1 foot .3048 meter 1 liquid quart -9465 liter 1 yard .9144 meter 1 gallon 3.86 liters 1 rod 5.029 meters 1 dry quart 1.101 liters 1 mile 1.6093 kilometers 1 peck 8.811 liters 1 square inch 6.452 sq. centimeters| 1 bushel 35.24 liters 1 square foot 1 square yard 1 square rod 1 acre 1 square mile 1 cubic inch 1 cubic foot 1 cubic yard .0929 sq. meter .8361 sq. meter 25.29 sq. meters .4047 hectare 259 hectares 16.39 cu. centimeters .02832 cu. meter .7646 cu. meter 1 ounce av’d’p 1 pound av’d’p 1 ton (2000 lbs.) 1 ton (2240 lbs.) 1 grain troy 1 ounce troy 1 pound troy 28.35 grams .4536 kilogram .9072 metric ton 1.016 metric ton .0648 gram 31.104 grams 3732 kilogram APPENDIX. 339 TABLE FOR THE CONVERSION OF Metric WriGHTs AND MrAsurEs INTO Cus- TOMARY UNITED STATES EQUIVALENTS AND THE REVERSE. From the legal equivalents are deduced the following tables for convert- ing United States weights and measures. METRIC TO CUSTOMARY. LinEAR MEASURE. Meters = Inches. Meters = Feet. Meters = Yards. Kilometers = Miles. 1= 39.37 1= 3.28087 1=1.093623 1=0.62137 2= 78.74 2= 6.56174 2=2.187246 2=1.24274 3=118.11 38= 9.84261 3 =3. 280869 3=1.86411 4=157.48 4=13.12348 4=4.374492 4=2.48548 5=196.85 5=16.40435 5=5.468175 5=3.10685 6 = 236. 22 6=19 68522 6 =6.561738 6=3.72822 7=275.59 7 =22.96609 7=7.655361 7=4.34959 8=314.96 8 = 26. 24696 8 =8.748984 8 =4.97096 9=354.33 9 = 29. 52783 9=9.842607 9 = 5.59233 CUSTOMARY TO METRIC, LinEAR MEASURE. inches = Centimeters. Feet = Meters. Meters = Yards. Miles = Kilometers. WOBNBWAPwWHe bid daed af ted NNER NONaANONG bo RS 1=0.304798 2=0.609596 3 =0.914393 Hidde de ded OONHD OP 0.914393 .828787 .743179 657574 .571966 486358 .400753 .315148 . 229537 ODBDNAWaPWWH iobod it tba DID OP why re ODNONPWN tidied dt toed eee PNR OWDDHWE .60935 21869 82804 .43739 04674 . 65608 . 26543 .87478 .48412 340 METRIC SYSTEM. Square Measure. Copic MEASURE. ae ob 3 g 2 Ei z : Z ee 26 ef eg e228 ot=o8 e8=oe Bs 5a B= Be Ba BA Be Be ae 25 wn Rn Nn n RQ n oO 1S) oO .S) 1=0.155 1=10.764 l= 1.196 1= 35.315 | 1=0.02832 2=0.310 2=21.528 2= 2.392 2= 70.631 | 2=0.05663 3=0.465 3 =32.292 3= 3.588 3=105.947 | 3=0.08495 4=0.620 4=43.055 4= 4.784 4=141.262 | 4=0.11326 5=0.775 5=53.819 5= 5.980 5=176.584 | 5=0.14158 6=0.930 6 =64. 583 6= 7.176 6=210.899 | 6=0.16990 7=1.085 7=75.347 7= 8.372 7 =247.209 | 7=0.19821 8=1.240 8=86.111 8= 9.568 8 = 282.525 | 8=0.22653 9=1.395 9=95.874 9=10.764 9=317.840 | 9=0.25484 Square Measure. Liquip Measure. £ vs (oF ae ee z 3 g : 4 Se 6 | Be Serer Ee a ee 3 = a n mn H QD N na oO & a [<7 a 1] 1= 6.452 | 1=0.09290} 1=0.836 1=0.338 | 1=1.0567| 1=0.26417 2=12.903 | 2=0.18581 | 2=1.672 2=0.676 | 2=2.1134|] 2=0.52834 3=19.354 | 3=0.27871 | 3=2.508 3=1.014 |3=3.1700} 3=0.79251 4=25.806 | 4=0.37161| 4=3 3-44 4=1.352 | 4=4.2267| 4=1.05668 5=32.257 | 5=0.46452] 5=4.181 5=1.691 | 5=5.2834] 5=1.32085 6 =38.709 | 6=0.55742| 6=5.017 6=2.029 | 6=6.3401] 6=1.58502 7=45.160 | 7=0.65032| 7=5.853 7=2.368 | 7=7.3968| 7=1.84919 8=51.612 | S=0.74823 | 8=6.689 8=2.706 | 8=8.4534} 8=2.11336 9=58 .063 | 9=0.83613 | 9=7.525 9=3.043 |9=9.5101} 9=2.37753 Dry Measure. Liquin Measure. 2 é gg 6 a x] 8 I 8 a a zg A 2-4 238 eae g = § ae: é ae a 5 a SG 2 OS Be Pg g <6 sae l= 2.8375 | 1=0.35242 1= 2.957 1=0.94636 | 1= 3.78544 2= 5.6750 | 2=0.70485 2= 5.915 | 2=1.89272 | 2= 7.57088 3= 8.5125 | 3=1.05727 3= 8.872 | 3=2.83908 | 3=11.35632 4=11.3500 | 4=1.40969 4=11.830 | +=3.38544 | 4=15.14176 5=14.1875 | 5=1.76211 5=14.787 | 5=4.33180 | 5=18.92720 6=17.0250 | 6=2.11454 6=17.744 | 6=5.67816 | 6=22.71264 7=19.8625 | 7=2.46696 7=20.702 | 7=6.62452 | 7=26.49808 8=22.7000 | 8=2.81938 8=23.659 | 8=7.57088 | 8 =30. 28352 9=25.5375 | 9=3.17181 9=26.616 | 9=8.51724 | 9=34.06896 APPENDIX. 341 Weicnt (AVOIRDUPOIS). a of, | 4. a oe wip g B- &3y B= $83 Ce zh 3 S 548 & 848 Ea 8S o o in (e) ie] AY = faa) 1=0.1649 | t2735,974 1= 2.20462 1=0.9842 2=0 3086 2= 70.548 2= 4.40924 2=1.9684 3=0.4630 3=105.822 3= 6.61386 3=2.9526 4=0.6173 4=141.096 4= 8.81849 4=3 9368 5=0.7716 5 =176.370 5=11.02311 5=4.9210 6 =0.9259 6=211.644 =13.22773 6=5.9052 7=1.0803 7 =246.918 7 =15. 43235 7=6. 8894 8=1.2346 8 = 282.192 $=17. 63697 8 =7.8736 9 =1.3889 9=317.466 | 9=19.84159 9 =8 8578 | 3 3 a | a = = e fil . : 2 1s Sia 4 264 E 2) 28 a7 a6 gaa” & ag! 2 0 ge! G6 o o 5 So] aa iva} ra] a 1= 6.4799 1= 28.3495 1=0.45359 1=1.0161 212.9598 2= 56.6991 2=0.90919 2=2 0321 3=19 4397 3= 85.0486 3=1.36078 3=3.0482 4=25.9196 4=113.3981 4=1.81437 4=4.0642 5 =32.3995 5=141.7476 5 =2.26798 5 =5.9803 6 =38.8793 6=170.0972 6=2.72156 6 =6.0963 7 =45.3592 7=198. 4467 7=3.17515 7=7.1124 8=51.8391 8 =226.7962 8 =3. 62874 8=8. 1284 9 =58.3190 9 =255.1457 9 = 4.08233 9=9 1445 II il INDEX. PAGE Abnormal! milky ahsg ones anactas fa cuihn stews okey tudinal: 54 Acid, butyric, capric, caprylic, myristic, oleic, palmitic, stearic......... 14 carbonic, hydrochloric, phosphoric, sulphuric. .................. 18 CLUB Ganz cried fete shalteng ade ys-tSens sir Rah ashen tina Dee) Seed naa ts 2c Se 20 VACUA Gis sone ey Syd te led tas an te cette tend N ic headlty oe Ba Rater ond 213 SANCVIICs caw .siarue hein dgin aathed nee ee BON aR Ea need gee eS 99 SU PRUPIC a, dst ahd Meedyo.e Stein Ral ranthieRe ameee wan Ay ne te lacich ain dae 2 85 lestsisieaceaedawa sivadende ve Ue Perak eee yd soa yous 80, 208, 206 Acidity of mille: .0 gescuiss veo deee Magi tdeeush due be kaa nuaewen oe de 78 of ripened cream in relation to richness of cream... ........... 209 OR StATCCTS) a pactawcs te oeie Ades nk oa ee eae Menon Sere tate e SERRE 223 COSESHOR sad shernoe cess Laeats Sees Sore sa iawn Sard aetang vod a ween Nien 208 Adhesion:of mil kes.cngctsenis ink Retna sa L ES Bh eee e eal Galena ee 37 Al buriven jin mike oss eased 2a dase es giviecas Gk Foe KR hend Gacedbla s aUeaea ah eae 16 Albuminoids inamilky 4.555 cess sieve aswlyaccaadndees dentese anak vals 14 Alkali of various strengths for measuring acid in milk and cream. ...... 80 Amphoteric reaction of milk... ......... 0.00 e eee cee eee ees 32 ANILISeptiesia4 hou eres ete de tasted aie ge wee Tea ba a adlen 48 Babeock test: for tats oa.6 15 we pated Wee ERG Aa ne PELE Calan 84 causes and remedies for common defects in clear- Ness Of fat Ny... ous tak ane haley ay wee wees Se 87 Bacteria in milk, aroma and flavor producing. ...............2.0eeeee 187 as a cause of deterioration of butter................. 11 Classification. Of, cu.a,< oe gesenad Ge Boehiwe dae wee Bs 50 conditions favoring development of... .............. 45 desirable and undesirable in cream ripening........... 189 number of, in milk. 2.0.0... ee eee 51 size and shape Of: 000s 00 sie adsee sane ee as dete ees 45 SOUPCES Ol ice gone siht ou Gaus edie eNotes turete emacs 52 unfavorable conditions for... ......... cece e eee eeeee 48 Biological changes in ripening cream............0.sesceeeeece eevee 210 Boiler, cleaning of, priming of........... 0.0... eee cece eee 332 firing with wood and coal..................0...02..00005. 330 344 INDEX, PAGE Breeds, composition of milk from various.............0.0.0e0000e- 68 Brine. for mechanical refrigeration............... 0.0.0.0 00s 327 properties of NaC] and CaCl............... 00.00.0000. .. 827 Brine, salting butter With... 0... ccc ccc cect ee eect eee ee eet eaeees 264 SOAKING TUDS Msg a.5-5-g: accu ten, Sai auacare wate a ib iia lots allaldv eoddarnd law ace 271 Butver, appearance Of:o. nic. caves coe dee came nae Sheed whee ewes 292 COlOT Oly. grt eee hag aie Wee a wnahnonahge ae ewe re ME AN 238, 291 COMpositioniol.. vavvawdauig bs 3s tence Shibiesy Beka ga unde aw 281 COst-Of MANUIACHUFING,. 34:6 ah le deca Paes Lacng gaeaeale dean eed 278 classification ard grades of, as outlined by N. Y. Mercantile Ex- CHANGE. Heals os Sey axReaeieesola anaes petiok s lalawee ean ten 292 exportation fy. svuhvadiaerenio ass dese ne oe Gl deen ae eea} 307 AMLAV ORIOL ics fice i beast hea ice ico aero Hiss Da tuess Me PAA tates S 290 judging and erading Ol... Sod ane eos board DR RE ee 286 keeping in creameries............. 2.0.0.0 0 ee .276, 310, 313, 314 making of OM Garm. 2.5 gost once iden sh eae we tele ee eee Gace ones 169 mottled, causes and remedy... ...... 0.0... cece cee cee eee 263 packing Of. sack s.faae pat eio Acasa de Raut eaneee ah Aaa toke nates 271, 275 PRINNG-O8, gary aoa as ae aM pans eae ee dplgae ey ees es 274 rancid; and Gause Ofs..+c6 cites dow nc hee eh we Be pee ee 11 SAUIMESS Of, “pie ve Pilea He aun away eon RAG saw HESS owes wa eae 292 SUOMING IM: Creame ries: s wy cals da duets bales Siang lnk eee obae 276 texture or bod yiGbn. ois ct Sin sh die tab w aa ntonels ebans Suhr decades 290 Test for Water Iii. piece. 8b een ae ste peed oes We we aged & oak 87 washing, and kind of wash-water.............0.....00000000.% 247 WMOTKING Offs cca ccna tls aid usu ses Dawe e NOR Ae Sundin ead eae 266 Birtbermi le, eines econ sce aa eacisea! S mardi oewn ae we wate a aie a cya ea bale 227, 232, 247 BATE PIU, hepa sicerts attteer eak wea tla Wanda epagtcdan pleut punadhee a & OW thecee "Gdns Benoa ee 13: Calculation of amount of salt to add to butter... .....0....0...00..000. 256 of average per cent fat... 2... ee cece eee eens 105 ofchurn yield) occis5 cede tenes da eae aed ouigek gine Se bade 109 of cream-raising coefficient........... 0.0.00... . cece eee ee 113 Of dividendsyis) oes cessed a euln HOG ceed ena etcniee Hee Ace abs 109 OP GVEITUMN g3c555 aie piesa aecanh Sores Se Rech eG, Ws doe Babe ONE Mes das 107 Of Solids milk 24504 alas Rh s se he bedemas aa eneye ene 35 of speed, pulleys, belts........ 0.0... 0c c cece e ee ee eee 331 Gans; Startersa ex oi pee be oe HEME on at SY sar ov nh aie ca hada a Baa eae 225 Care:Of Créam: ON Parise ic 2 incie dk Suse s a ek aed dw Se aes Aate aes, 158 Caseinin milk:,COnGIitION Of... i020 .a0eses seen Sears peed nce ews 15 Centrifugal separation of cream. .... 2.0... 0.0... c eee eee ee 129 Changes in milk and cream, chemical, physical, and biological.......... 210 Chemical changes in ripe and over-ripe cream..................... 218, 215 Churn, keeping in good condition..................... i Blenieie, pane dia dik 245 Churn yield, calculation of............. 0.000000. e cece 109 Churned milk, sampling... 0.2.2.0... 000 cece ccc e cece cc cee eee nneeuue 96 INDEX, 345 . PAGE Churning, amount of cream for a........00 00.00 c cece cccececcececeee 233 conditions affecting............000. 0.0 cece cece eee ce ev eeee. 227 efi tON fi iis vets ened x Acta aie cody cisada bea gat whupnnd- dea oar atea 226 difficult, causes and remedy for..........0..0..eeceeeecees 243 Churning mixed, sweet, and sour cream.......0.cceccecccececccceces 243 nature of agitation for... 2.2.0... cece eee eee ences 235 richness of cream for... 00.00.0000. c ccc eevee ceeeeueees 231 straining of cream previous to. ............00.0 ce. 00 ween 238 WHEN: TOMStO Pe ciateas Gusher uaius parte han 'ychaws wbametien mimes areas £39 Crtticacid an: mikes oss tasnnaeusawasiouage sun wns causes tien oes 20 Coal, daily weighing of. 2.0.00... 00000 oan Bod slack vs. lump-coal. 0... 0... cece eee uee 331 COLOR, DUG CEB ag eed ny aici al alaan nat aren aialle gate western eile Pela linden 238 Coloring matter in MilK.i. 6 oe ek ee ee eee ee seen ne 20, 31 Composite Samples. 6s Gveaaices da dbeae eae amnndalaiveteennseena 99 care and arrangement of. .................-...0.. 102 préservatives: fors ¢eudide decease ce eke eaain poke nes 99 sampling apparatus for... 0. .........00 0000 cece ee 94 Compositionof butter: 5.20052 Fk unl depen te des oe eran ean alee ae & 281 of colostrumiamilkycs aud ates atin Anes cucakn sa Ween BoEee 54 of dairy Saltss 223... aaah aa py toe the ee eae ha 262 of different kinds of milk. ........0.0. 000.0 cece eee eee 2 effect of, on quality of butter.......................008. 281 ofsalty milks. Geen ince tate nesse sia raG-pe sa Same dates 55 of separator slimes. y0855 cue nae wa clab ee ee ea eRe PETA Bea aes 144 of tuberculous milky... css cee sce eg epee se Ge tee ee dhe wen 62 Commercial starters... 61.6. cece eee teen nee 217 preparation and use of...........0.... 00. c eee eee 218 Continuous method of pasteurization. .. 6.2.2... eee eee 173 “Cooley”? method of cream separation. ..........600 00 eee 124 Cooling facilities, water, ice, mechanical refrigeration ........... 309 cost of natural ice-system vs. mechanical refrigeration ....... 310 SY SUCIUISR: 2 4148 id Sr, tiaras bhiady Syietin d fase Bigeay mae Aare Atenas Reece ane oe 309 Cows, average production Of... 0.0.06. 0 cece eee teenies 66 breeds Of saka idee nen ON TE Rae ERIN REM a sad es Tee das 68 costcof keepini@sid sia ansuawedens ee wna dee dok estes aac ale Sade boa 66 table showing profit and loss in keeping. .....-...-.+.....00005 67 Cream, acidity of, for churning......-... 0... 600. e eee eee eee eee 205 Care :of On fatitiy ss Guctted oboe ee Oe ee eR oe ese eee te ee et 158 effect of cleanliness on quality of... 0.6.0.0... 0. ee eee eee eens 159 grading Of... ..... 0. eee eee eee eee een ees 79 methods of disposing of... ...... 6.0022 e eee eee eee 167 mixing of different qualities. ........... 0.00. ee eee eee eee eee 202 pasteurization OL eile sash fo eRe RO el NE AT ies 173, Of SOUT sae AE ER Sasa bee GE REP Rae 186 346 INDEX, PAGE Cream, Tipeping Of s..s2.0 soe nus GAs Hla Lae Zaeds Foe AR 187 SAME LIME OL shes vaye tie ase doarteate s soeineet duo Site oe opt sar naalalepenanels AGiedar a. wyatt 93 Specific heat Ofva sas eens gion ia seas Gl om tele awa bed aGeey WANES 38 Creamery sewage disposal. 0.0.0.0... 0 cece ccc eee eet e eens 278 plans: « aia seve wes ecley ev Hate ede sie eae 276 Deep-setting system of cream separation. ........ 0. cece cece eee ee aes 124 Difficult churning, causes and remedy.......... 0.00. s eee eeeeeeeeeeee 243 Dilution, effect of, on creaming ........ 00. eee ee eee eee eee tees 128 DISINFECHAM ES’. 3 ci5 sie C51 Bad Seg RES Sede CRE Mea A 6 bod CV Rama oh eee BE 48, 99, 246 Electricity, effect of, on germs in milk... ....... 2... cece eee eee eee 53 TEnzynoesnamilly: 344 can cirag Ha neg ue ee aken gee es Geechee od Mee aA Eh w 20 effect: of heat (One ois. daxivareece sexes aes eee sss 41 tests: fob uo eh abs aie erga Be ere eR oo wee Es 42 EX POLtS OF PULTE: coe ilicaiaedaciny Suabled caminei ade ewe haouingty meeanieds 296 Hattoriess plan. Ofyc 9 4 auxtee sed ee sabia wk Gaye alee ae ka a ew alee aa 279 Harrington’ tesbives sain sed apes 84 od tia oe Wes SSRN GER eo Dado 208 Prarteam: Diatte re oo dik seen iiss a dsb ls chee abe astarghaee aie eoeelare t drane won casera aula derd 286 BOTAN ie dos alls 8 Galan ah asthe mueae' lace gran ae Mate Wes BGS oa Balog Be eee, 5 ComPOsiion Ol. a tica wie yee Se Reg ENS HME Ae ete 13 CONGIION! Office ¢ coujh weddeys nas PRAT Ae ooh ede as eae 6 effects of environment....... 0.0... cece cece cece eee aes 76 OPES ON: pide se disc Adnan e miata a duaaeha mee aansee Balas 42 of various feeds on composition of................. 75 PY CONICS Oy. apn scream organ Ge Monga Wade sealed en Meek ees 8 BLY CErING: IMs nibs ccna stants sya Sanne and Ne Gal Moaanhoul tics 14 melting-point Of; . nec 8c csi ev erage essai dessins snwnssane 12 membrane enveloping fat globules. ...................... 9 microscopical appearance Of............. 000000000 cece 6 THOMAVOLOt Gy tie cps 526 ade tna cage ee 4 labs de mp cove Sain Shs alah EG 12 paying for, as compared with fat in cream................ 116 Separation Of. sacunsieset aa wteens Oe ee nae ee se we Mas ese nak 123 size of globuleSiiss. dss. ge een ge see Se0es ws aw dude ake e dme a 7 testing 1Ors. cuss aoa vanes Henk pee es hl ae mannds wp emeneaes 84 Volatiless ysis ered « chesnounaeaasayeact Wlnsaea ene tneeiy dadeceradalneee 11 Feeds, effects on milk. ..... 0.0.0... cece ccc cece cece een eeneeeue 75 Hermentsinin mille, coe aso eae ad bey oedema dg sad whedon econ 44 CLASSES: Of oii. dea dce anecy a s ey owe herd eis adeea lee a Bb Sv 44, 49 favorable and unfavorable condition for........... 45, 48 Fermentations, detection of ..... 0.0.6... 00. cece cece eee ee eens 56, 81 various kinds of... 6.0... 01. cece cece cece cease 44, 55 Filtration Of waters oi. cc doe y cbee saa AY seine eee eee oa wee ae ae 250 INDEX, at PAGE Firing the boiler... 2... ccc ccc cee cece eceece ceed 329 wood vs. coal, comparative cost of............0...0.-e ce ues 330 Flavors-of: butters < sis .csew ae wat ecdedcdsaaincaresa nea a Aare bk Sleek ee 290 OE TAM sb, sate centre W's aces a aga ale ag G76 We 'e a Ben ba eR Raa 18, 30, 40 ‘Food for bacteniay asi :460 cia bg te athe eng See einen dave ral Calculus Large 12mo, r vol. Curve Tracing in Cartesian Co-ordinates eacirbiccgn tata. ds Was Acoelanels fy, 12mo, Differential Equations 4s eceeo v's adnan & ee eae sieves worse . 8v0. Elementary Treatise on Differential Calculus ........... Large 12mo, Elementary Treatise on the Integral Calculus....... ... Large 12mo, 2 Theoretical Mechanics.... ......... ised girnlans PEZMNOS Theory of Errors and the “Method of Least Squares. av ariovantrliaheg en sat 12mo, Treatise on Differential Calculus......................, Large 12mo, Treatise on the Integral Calculus.............-........ Large 12mo, Treatise on Ordinary and Partial Differential Equations..Large 12mo, 12 NNNH HARD I wWwnNH AN NW AW WADHNWTDY HHH HH NRHN AYA Nu WOWWHWH He MD fate} oye) oo EO 50 5° 50 50 co 50 tele) 50 vo 00 50 00 50 50 50 fete} 50 00 foto) 50 50 00 oo 00 rele) 50 50 25 50 fore) 50 75 50 fete) 15 00 25 00 50 00 oo 50 50 90 50 00 oo 50 Laplace’s Philosophical Essay on Probabilities. 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